CN102042712A - Backheating type absorption-generation system and multiterminal heat-supply third-class absorption heat pump - Google Patents

Backheating type absorption-generation system and multiterminal heat-supply third-class absorption heat pump Download PDF

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CN102042712A
CN102042712A CN2010106124989A CN201010612498A CN102042712A CN 102042712 A CN102042712 A CN 102042712A CN 2010106124989 A CN2010106124989 A CN 2010106124989A CN 201010612498 A CN201010612498 A CN 201010612498A CN 102042712 A CN102042712 A CN 102042712A
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李华玉
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems

Abstract

The invention provides six backheating type absorption-generation systems and a series of multiterminal heat-supply third-class absorption heat pumps, belonging to the technical field of absorption heat pumps.A first absorber, a second absorber, an an absorption-generation device and a first generator or additionally a second generator, a plurality of solution pumps, a plurality of solution heat exchangers and a vapor separation room are used as main components; a single-loop solution cycle or double-loop solution cycle is adopted, and the second generator and the second absorber, or the first generator and the second absorber form a backheating process; the absorption-generator and the vapor separation room form a solution generation process under the action of a second-class driving force; the first generator alone or along with the second generator forms a solution generation process under the action of a first-class driving force, thus forming the backheating type absorption-generation system; and the addition of a first condenser, a second condenser, a first evaporator or additionally a second evaporator, a throttling valve and a refrigerant liquid pump can form a full-series multiterminal heat-supply third-class absorption heat pumps based on the backheating type absorption-generation system.

Description

Back-heating type absorption-generation systems and multiterminal heat supply the 3rd class absorption heat pump
Technical field:
The invention belongs to low temperature exhaust heat utilization and technical field of heat pumps.
Background technology:
The 3rd class absorption heat pump between several of different effects or different progression, their running parameter interval is disjunct, and bigger difference is arranged on performance index especially.
From workflow, for improving the highest heat supply temperature of the 3rd class absorption heat pump, key is to reduce the solution concentration that enters generator; In order to utilize the more waste heat of low temperature, key is to improve the solution concentration that enters absorber.If can take rational technical measures, improve the solution concentration that enters absorber simultaneously and reduce the solution concentration that enters generator, and the amplitude that can select solution concentration to reduce and improve within the specific limits according to demand, this will have very important meaning.
In order to promote the heat supply temperature of the 3rd class absorption heat pump, make it have between higher performance index and the realization running parameter and the linking of the free of discontinuities between the performance index, the present invention adopts flow process cleverly, the backheat principle is applied to the absorption-generating process of solution, increase by second absorber as the backheat high-temperature heat supply end, set up back-heating type absorption-generation systems, and obtain the different numbers of imitating based on this, multiterminal heat supply the 3rd class absorption heat pump of different progression, this will make all corresponding the 3rd class absorption heat pump in each running parameter interval, realize the serialization of the 3rd class absorption heat pump on the running parameter interval, realize the serialization of the 3rd class absorption heat pump on performance index.
Summary of the invention:
Main purpose of the present invention provides back-heating type absorption-generation systems and multiterminal heat supply the 3rd class absorption heat pump, is divided into six kinds of back-heating type absorption-generation systems and based on a series of multiterminal heat supply the 3rd class absorption heat pumps of back-heating type absorption-generation systems.Concrete summary of the invention subitem is described below:
1. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, the 3rd solution heat exchanger and branch steam chest are formed, first absorber has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger, absorption-generator also has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger, first generator also has the concentrated solution pipeline to be communicated with dividing steam chest through first solution heat exchanger and absorption-generator, divide steam chest to also have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger, first absorber also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber also has heated medium pipeline and external communications, second generator also has the refrigerant vapour passage and the second absorber connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest to also have refrigerant vapour passage and external communications, absorption-generator also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms single channel solution and loops back hot type absorption-generation systems; Wherein, when not having second generator and the 3rd solution heat exchanger, second generator has the refrigerant vapour passage to be communicated with second absorber to change to first generator to increase the refrigerant vapour passage to be communicated with second absorber, the branch steam chest have the concentrated solution pipeline through second solution pump and the 3rd solution heat exchanger be communicated with second generator, second generator has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger to change to the branch steam chest and have the concentrated solution pipeline to be communicated with first absorber through second solution pump again.
2. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, the 3rd solution heat exchanger and branch steam chest are formed, first absorber has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with dividing steam chest through second solution heat exchanger and absorption-generator, divide steam chest to also have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger, absorption-generator also has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger, first generator also has the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger, first absorber also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber also has heated medium pipeline and external communications, second generator also has the refrigerant vapour passage and the second absorber connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest to also have refrigerant vapour passage and external communications, absorption-generator also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms two-way solution and loops back hot type absorption-generation systems; Wherein, when not having second generator and the 3rd solution heat exchanger, second generator has the refrigerant vapour passage to be communicated with second absorber to change to first generator to increase the refrigerant vapour passage to be communicated with second absorber, the branch steam chest have the concentrated solution pipeline through second solution pump and the 3rd solution heat exchanger be communicated with second generator, second generator has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger to change to the branch steam chest and have the concentrated solution pipeline to be communicated with first absorber through second solution pump again.
3. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and branch steam chest are formed, first absorber has the weak solution pipeline to be communicated with absorption-generator, absorption-generator also has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger, first generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with dividing steam chest through second solution heat exchanger and absorption-generator, divide steam chest to also have the concentrated solution pipeline to be communicated with first absorber through second solution pump, first absorber also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber also has heated medium pipeline and external communications, second generator also has the refrigerant vapour passage and the second absorber connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest to also have refrigerant vapour passage and external communications, absorption-generator also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms single channel solution and loops back hot type absorption-generation systems; Wherein, when not having second generator, second generator has the refrigerant vapour passage to be communicated with second absorber to change to first generator to increase the refrigerant vapour passage to be communicated with second absorber, first generator have the concentrated solution pipeline through first solution heat exchanger be communicated with second generator, second generator has the concentrated solution pipeline to be communicated with the branch steam chest through second solution heat exchanger and absorption-generator to change to first generator and have the concentrated solution pipeline to be communicated with the branch steam chest through first solution heat exchanger, second solution heat exchanger and absorption-generator again.
4. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, divide steam chest and solution choke valve to form, first absorber has the weak solution pipeline to be communicated with dividing steam chest through solution choke valve and absorption-generator, divide steam chest to also have the concentrated solution pipeline to be communicated with first absorber through second solution pump, absorption-generator also has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger, second absorber also has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger, first generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger, second generator also has the concentrated solution pipeline to be communicated with absorption-generator through second solution heat exchanger, first absorber also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber also has heated medium pipeline and external communications, second generator also has the refrigerant vapour passage and the second absorber connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest to also have refrigerant vapour passage and external communications, absorption-generator also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms two-way solution and loops back hot type absorption-generation systems; Wherein, when not having second generator, second generator has the refrigerant vapour passage to be communicated with second absorber to change to first generator to increase the refrigerant vapour passage to be communicated with second absorber, first generator have the concentrated solution pipeline through first solution heat exchanger be communicated with second generator, second generator has the concentrated solution pipeline to be communicated with absorption-generator through second solution heat exchanger to change to first generator and have the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger again.
5. multiterminal heat supply the 3rd class absorption heat pump, be described at the 1st, absorption-generator does not have in the back-heating type absorption-generation systems of heated medium pipeline and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through choke valve, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein: 1. can select have the cryogen liquid pipeline to be communicated with second evaporimeter second condenser and be adjusted into second condenser and have the cryogen liquid pipeline to be communicated with first evaporimeter, increase by second choke valve again and set up the cryogen liquid pipeline and be communicated with second evaporimeter through second choke valve by first evaporimeter through the cryogen liquid pump through the cryogen liquid pump; When 2. not having second evaporimeter, have the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump second condenser and be adjusted into second condenser and have the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator.
6. multiterminal heat supply the 3rd class absorption heat pump, be described at the 1st, absorption-generator has in the back-heating type absorption-generation systems of heated medium pipeline and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the first throttle valve, first evaporimeter also has the cryogen liquid pipeline to be communicated with second evaporimeter through second choke valve, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter or first evaporimeter through the cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter, having the cryogen liquid pipeline to be communicated with second evaporimeter or first evaporimeter through the cryogen liquid pump second condenser is defined as second condenser and has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, cancel the cryogen liquid pipeline that first evaporimeter is communicated with second evaporimeter through second choke valve, first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator.
7. multiterminal heat supply the 3rd class absorption heat pump, be in the 2nd described back-heating type absorption-generation systems, when 1. second generator and the 3rd solution heat exchanger are arranged, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through choke valve, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter, have the cryogen liquid pipeline to be communicated with second evaporimeter through choke valve first condenser and be adjusted into first condenser and have the cryogen liquid pipeline to be communicated with first evaporimeter through choke valve, first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator; When 2. not having second generator and the 3rd solution heat exchanger, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the first throttle valve, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, first evaporimeter also has the cryogen liquid pipeline to be communicated with second evaporimeter through second choke valve, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter and second choke valve, cancel the cryogen liquid pipeline that first evaporimeter is communicated with second evaporimeter through second choke valve, first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator.
8. multiterminal heat supply the 3rd class absorption heat pump, be described at the 3rd, absorption-generator does not have in the back-heating type absorption-generation systems of heated medium pipeline and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve, cryogen liquid pump and solution choke valve, first absorber had the weak solution pipeline to be communicated with absorption-generator to be adjusted into first absorber has the weak solution pipeline to be communicated with absorption-generator through the solution choke valve, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through choke valve, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein: 1. can select have the cryogen liquid pipeline to be communicated with second evaporimeter second condenser and be adjusted into second condenser and have the cryogen liquid pipeline to be communicated with first evaporimeter, increase by second choke valve again and set up the cryogen liquid pipeline and be communicated with second evaporimeter through second choke valve by first evaporimeter through the cryogen liquid pump through the cryogen liquid pump; When 2. not having second evaporimeter and solution choke valve, having the cryogen liquid pipeline to be communicated with second evaporimeter through the cryogen liquid pump second condenser is adjusted into second condenser and has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, first absorber has the weak solution pipeline to be communicated with absorption-generator, and first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator.
9. multiterminal heat supply the 3rd class absorption heat pump, be described at the 3rd, absorption-generator has in the back-heating type absorption-generation systems of heated medium pipeline and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve, cryogen liquid pump and solution choke valve, first absorber had the weak solution pipeline to be communicated with absorption-generator to be adjusted into first absorber has the weak solution pipeline to be communicated with absorption-generator through the solution choke valve, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the first throttle valve, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter or second evaporimeter through the cryogen liquid pump, first evaporimeter also has the cryogen liquid pipeline to be communicated with second evaporimeter through second choke valve, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter and solution choke valve, having the cryogen liquid pipeline to be communicated with first evaporimeter or second evaporimeter through the cryogen liquid pump second condenser is defined as second condenser and has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, cancel the cryogen liquid pipeline that first evaporimeter is communicated with second evaporimeter through second choke valve, first absorber has the weak solution pipeline to be communicated with absorption-generator, and first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator.
10. multiterminal heat supply the 3rd class absorption heat pump, be in the 4th described back-heating type absorption-generation systems, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator in first generator has the refrigerant vapour passage to be communicated with first condenser, first condenser also has the cryogen liquid pipeline to be communicated with second evaporimeter through choke valve, to absorb-generator has refrigerant vapour passage and external communications to be defined as second evaporimeter has the refrigerant vapour passage to be communicated with absorption-generator, to divide steam chest to have refrigerant vapour passage and external communications to be defined as the branch steam chest has the refrigerant vapour passage to be communicated with second condenser, second condenser also has the cryogen liquid pipeline to be communicated with first evaporimeter through the cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first evaporimeter first absorber has the refrigerant vapour passage to be communicated with first absorber, first condenser also has heated medium pipeline and external communications, second condenser also has cooling medium pipeline and external communications, first evaporimeter and second evaporimeter also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter, have the cryogen liquid pipeline to be communicated with second evaporimeter through choke valve first condenser and be adjusted into first condenser and have the cryogen liquid pipeline to be communicated with first evaporimeter through choke valve, first evaporimeter increases the refrigerant vapour passage and is communicated with absorption-generator.
11. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to converge through newly-increased solution heat exchanger and the concentrated solution pipeline of first generator after first solution heat exchanger, be communicated with dividing steam chest through absorption-generator again, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
12. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
13. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-10 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
14. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator with dividing steam chest to be communicated with to be adjusted into first generator in first generator through increasing solution heat exchanger newly through first solution heat exchanger and absorption-generator, newly-increased generator also has the concentrated solution pipeline to be communicated with dividing steam chest through first solution heat exchanger and absorption-generator, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through first solution pump, first solution heat exchanger and newly-increased solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
15. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through first solution pump, first solution heat exchanger and newly-increased solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
16. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, first solution heat exchanger and newly-increased solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, first solution heat exchanger and newly-increased solution heat exchanger are communicated with first generator, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with newly-increased generator through increasing solution heat exchanger newly with dividing steam chest to be communicated with to be adjusted into first generator, newly-increased generator also has the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
17. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, first solution heat exchanger and newly-increased solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, first solution heat exchanger and newly-increased solution heat exchanger are communicated with first generator, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
18. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with newly-increased generator through first solution pump and first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased solution pump and newly-increased solution heat exchanger, there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing solution heat exchanger newly with dividing steam chest to be communicated with to be adjusted into first generator in first generator through first solution heat exchanger and absorption-generator, first solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
19. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with newly-increased generator through first solution pump and first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with absorption-generator through the newly-increased solution heat exchanger and first solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
20. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased generator through first solution pump and first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with second generator through the newly-increased solution heat exchanger and first solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with second generator through newly-increased solution heat exchanger; When 2. not having second generator, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased generator through first solution pump and first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased solution pump and newly-increased solution heat exchanger, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline through increasing solution heat exchanger newly with dividing steam chest to be communicated with to be adjusted into first generator, first solution heat exchanger, second solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with dividing steam chest through newly-increased solution heat exchanger, second solution heat exchanger and absorption-generator.
21. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased generator through first solution pump and first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with second generator through the newly-increased solution heat exchanger and first solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with second generator through newly-increased solution heat exchanger; When 2. not having second generator, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased generator through first solution pump and first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with absorption-generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have the refrigerant vapour passage to be communicated with the newly-increased generator in back with newly-increased generator in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with absorption-generator through the newly-increased solution heat exchanger and second solution heat exchanger.
22. multiterminal heat supply the 3rd class absorption heat pump, be in described at the 11-21 item, that second generator is arranged multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased second choke valve, second generator had drive thermal medium pipeline and external communications and be adjusted into first generator and set up the refrigerant vapour passage and is communicated with back second generator with second generator and has cryogen liquid pipeline warp to increase second choke valve newly again to be communicated with formation single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump with first condenser.
23. multiterminal heat supply the 3rd class absorption heat pump, be in described at the 11-21 item, as not have second generator multiterminal heat supply the 3rd class absorption heat pump, there is the refrigerant vapour passage to be communicated with to be adjusted into newly-increased first generator to set up the refrigerant vapour passage in first generator and is communicated with, formation single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump with second absorber with second absorber.
24. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with newly-increased second generator through newly-increased second solution heat exchanger with the newly-increased first generator connected sum through newly-increased first solution heat exchanger respectively, newly-increased first generator has the concentrated solution pipeline through having the concentrated solution pipeline all to converge with the concentrated solution pipeline of first generator after first solution heat exchanger with newly-increased second generator after newly-increased first solution heat exchanger after newly-increased second solution heat exchanger, be communicated with dividing steam chest through absorption-generator again, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
25. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with newly-increased second generator through newly-increased second solution heat exchanger with the newly-increased first generator connected sum through newly-increased first solution heat exchanger respectively, newly-increased first generator also has the concentrated solution pipeline to be communicated with absorption-generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with absorption-generator through newly-increased second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
26. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-10 item, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump is set up the weak solution pipeline and is communicated with newly-increased second generator through newly-increased second solution heat exchanger with the newly-increased first generator connected sum through newly-increased first solution heat exchanger respectively, newly-increased first generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to converge with the concentrated solution pipeline of first generator after first solution heat exchanger after newly-increased second solution heat exchanger, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
27. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased first generator with dividing steam chest to be communicated with to be adjusted into first generator in first generator through first solution heat exchanger through first solution heat exchanger and absorption-generator, newly-increased first generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with dividing steam chest through newly-increased second solution heat exchanger and absorption-generator, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through first solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and first solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
28. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased first generator through first solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with absorption-generator through newly-increased second solution heat exchanger, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through first solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and first solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
29. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased first generator through first solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased second solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and first solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with newly-increased first generator through first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, newly-increased first generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline through newly-increased second solution heat exchanger, second solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and first solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
30. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased first generator through first solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with second generator through newly-increased second solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and first solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased first generator through first solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with newly-increased second generator through newly-increased first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with absorption-generator through newly-increased second solution heat exchanger and second solution heat exchanger, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and the weak solution pipeline is arranged through first solution pump, newly-increased second solution heat exchanger, newly-increased first solution heat exchanger and first solution heat exchanger are communicated with first generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
31. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with newly-increased second generator through first solution pump and first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased first solution pump and newly-increased first solution heat exchanger, there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing first solution heat exchanger newly with dividing steam chest to be communicated with to be adjusted into first generator in first generator through first solution heat exchanger and absorption-generator, newly-increased second solution heat exchanger, first solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
32. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with newly-increased second generator through first solution pump and first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased first solution pump and newly-increased first solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger and first solution heat exchanger are communicated with absorption-generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
33. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump and first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased first solution pump and newly-increased first solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger and first solution heat exchanger are communicated with second generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with second generator through newly-increased first solution heat exchanger and newly-increased second solution heat exchanger; When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump and first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased first solution pump and newly-increased first solution heat exchanger, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline through increasing first solution heat exchanger newly with dividing steam chest to be communicated with to be adjusted into first generator, newly-increased second solution heat exchanger, first solution heat exchanger, second solution heat exchanger and absorption-generator are communicated with dividing steam chest, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with dividing steam chest through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, second solution heat exchanger and absorption-generator.
34. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump and first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased first solution pump and newly-increased first solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger and first solution heat exchanger are communicated with second generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with second generator through newly-increased first solution heat exchanger and newly-increased second solution heat exchanger; When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump and first solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased first generator through newly-increased second solution pump and newly-increased second solution heat exchanger, newly-increased first generator also has the concentrated solution pipeline to be communicated with first generator through newly-increased first solution pump and newly-increased first solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, first solution heat exchanger and second solution heat exchanger are communicated with absorption-generator, having the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator to have refrigerant vapour passage and newly-increased first generator to be communicated with newly-increased first generator in back in first generator has the cryogen liquid pipeline to be communicated with first condenser through newly-increased first throttle valve again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, newly-increased first generator also has the refrigerant vapour passage to be communicated with newly-increased second generator in back with newly-increased second generator has newly-increased second choke valve of cryogen liquid pipeline warp to be communicated with first condenser again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, newly-increased second generator also has the refrigerant vapour passage to be communicated with first condenser, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger, second absorber has the weak solution pipeline to be communicated with newly-increased second generator through first solution pump, and first generator has the concentrated solution pipeline to be communicated with absorption-generator through newly-increased first solution heat exchanger, newly-increased second solution heat exchanger and second solution heat exchanger.
35. multiterminal heat supply the 3rd class absorption heat pump, be in described at the 24-34 item, that second generator is arranged multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve, second generator had drive thermal medium pipeline and external communications and be adjusted into first generator and set up the refrigerant vapour passage and is communicated with back second generator with second generator and has cryogen liquid pipeline warp to increase the 3rd choke valve newly again to be communicated with formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with first condenser.
36. multiterminal heat supply the 3rd class absorption heat pump, be in described at the 24-34 item, that second generator is arranged multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve, second generator had drive thermal medium pipeline and external communications and be adjusted into newly-increased first generator and set up the refrigerant vapour passage and is communicated with back second generator with second generator and has cryogen liquid pipeline warp to increase the 3rd choke valve newly again to be communicated with formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with first condenser.
37. multiterminal heat supply the 3rd class absorption heat pump, be in described at the 24-34 item, as not have second generator multiterminal heat supply the 3rd class absorption heat pump, there is the refrigerant vapour passage to be communicated with to be adjusted into newly-increased first generator to set up the refrigerant vapour passage in generator and is communicated with, formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with second absorber with second absorber.
38. multiterminal heat supply the 3rd class absorption heat pump, be in described at the 24-34 item, as not have second generator multiterminal heat supply the 3rd class absorption heat pump, there is the refrigerant vapour passage to be communicated with to be adjusted into newly-increased second generator to set up the refrigerant vapour passage in generator and is communicated with, formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with second absorber with second absorber.
39. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger again, to divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger is adjusted into the branch steam chest and the concentrated solution pipeline is arranged through second solution pump, newly-increased second solution heat exchanger and the 3rd solution heat exchanger are communicated with second generator 5, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorptions-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger again, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with first absorber through second solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorptions-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
40. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through the 3rd solution heat exchanger, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with first absorber through newly-increased solution pump and newly-increased solution heat exchanger again, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and the weak solution pipeline is arranged through newly-increased solution heat exchanger, the 3rd solution pump and second solution heat exchanger are communicated with second absorber, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorptions-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through second solution pump, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with first absorber through newly-increased solution pump and newly-increased solution heat exchanger again, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and the weak solution pipeline is arranged through newly-increased solution heat exchanger, the 3rd solution pump and second solution heat exchanger are communicated with second absorber, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorptions-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
41. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger again, to divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger is adjusted into the branch steam chest and the concentrated solution pipeline is arranged through second solution pump, newly-increased second solution heat exchanger and the 3rd solution heat exchanger are communicated with second generator 5, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger again, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with first absorber through second solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
42. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through the 3rd solution heat exchanger, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with first absorber through newly-increased solution pump and newly-increased solution heat exchanger again, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and the weak solution pipeline is arranged through newly-increased solution heat exchanger, the 3rd solution pump and second solution heat exchanger are communicated with second absorber, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through second solution pump, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with first absorber through newly-increased solution pump and newly-increased solution heat exchanger again, having the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger first absorber is adjusted into first absorber and the weak solution pipeline is arranged through newly-increased solution heat exchanger, the 3rd solution pump and second solution heat exchanger are communicated with second absorber, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
43. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with absorption-generator directly or through the solution choke valve first absorber is adjusted into first absorber and has weak solution pipeline warp to increase solution heat exchanger newly to be communicated with newly-increased absorption-evaporimeter, newly-increased absorption-evaporimeter has the weak solution pipeline directly or through the solution choke valve to be communicated with absorption-generator again, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with first absorber through second solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorptions-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
44. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, cancellation solution choke valve, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with absorption-generator directly or through the solution choke valve first absorber is adjusted into first absorber and has weak solution pipeline warp to increase solution heat exchanger newly to be communicated with absorption-generator, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through second solution pump, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with first absorber through newly-increased solution pump and newly-increased solution heat exchanger again, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorptions-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
45. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, there is the weak solution pipeline to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter with dividing steam chest to be communicated with to be adjusted into first absorber first absorber through increasing solution heat exchanger newly through solution choke valve and absorption-generator, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with dividing steam chest through solution choke valve and absorption-generator again, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with first absorber through second solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
46. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through second solution pump, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with first absorber through newly-increased solution pump and newly-increased solution heat exchanger again, cancellation solution choke valve, there is the weak solution pipeline to have the weak solution pipeline to be communicated with the branch steam chest with dividing steam chest to be communicated with to be adjusted into first absorber first absorber through newly-increased solution heat exchanger and absorption-generator through solution choke valve and absorption-generator, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
47. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased absorber with dividing steam chest to be communicated with to be adjusted into first generator in first generator through first solution heat exchanger through first solution heat exchanger and absorption-generator, newly-increased absorber also has the weak solution pipeline to be communicated with dividing steam chest through newly-increased solution heat exchanger and absorption-generator, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through first solution pump, the newly-increased solution heat exchanger and first solution heat exchanger are communicated with first generator, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
48. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through first solution pump, the newly-increased solution heat exchanger and first solution heat exchanger are communicated with first generator, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber.
49. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger, there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing solution heat exchanger newly with dividing steam chest to be communicated with to be adjusted into second generator in second generator through second solution heat exchanger and absorption-generator, second solution heat exchanger and absorption-generator are communicated with dividing steam chest, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased absorber, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, newly-increased absorber also has the weak solution pipeline to be communicated with dividing steam chest through second solution heat exchanger and absorption-generator, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
50. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with absorption-generator through the newly-increased solution heat exchanger and second solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber.
51. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with newly-increased absorber through first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first generator through the newly-increased solution pump and first solution heat exchanger, there is the concentrated solution pipeline concentrated solution pipeline to be arranged through first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator in first generator through first solution heat exchanger and absorption-generator, newly-increased solution heat exchanger and absorption-generator are communicated with dividing steam chest, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
52. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, to absorb-generator has the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger to be adjusted into absorption-generator and to have the weak solution pipeline to be communicated with newly-increased absorber through first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first generator through the newly-increased solution pump and first solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber.
53. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first generator through the newly-increased solution pump and first solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first generator through the newly-increased solution pump and first solution heat exchanger, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline through first solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, newly-increased solution heat exchanger, second solution heat exchanger and absorption-generator are communicated with dividing steam chest, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
54. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first generator through the newly-increased solution pump and first solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with second generator through first solution heat exchanger and newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first generator through the newly-increased solution pump and first solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and the concentrated solution pipeline is arranged through first solution heat exchanger, the newly-increased solution heat exchanger and second solution heat exchanger are communicated with absorption-generator, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber.
55. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, to divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorber through second solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and the 3rd solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger and newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorber through second solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
56. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, to divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorber through second solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and the 3rd solution heat exchanger, having the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger and newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter or second condenser set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, to divide steam chest to have the concentrated solution pipeline to be communicated with first absorber through second solution pump is adjusted into the branch steam chest and has the concentrated solution pipeline to be communicated with newly-increased absorber through second solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first absorber through newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter or second condenser set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
57. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased absorber with dividing steam chest to be communicated with to be adjusted into second generator in second generator through second solution heat exchanger through second solution heat exchanger and absorption-generator, newly-increased absorber also has the weak solution pipeline to be communicated with dividing steam chest through newly-increased solution heat exchanger and absorption-generator, to absorb-generator has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through the 3rd solution pump, the newly-increased solution heat exchanger and second solution heat exchanger are communicated with second absorber, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, first generator there is the concentrated solution pipeline through first solution heat exchanger, second solution heat exchanger and absorption-generator have the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger and second solution heat exchanger with dividing steam chest to be communicated with to be adjusted into first generator, newly-increased absorber also has the weak solution pipeline to be communicated with dividing steam chest through newly-increased solution heat exchanger and absorption-generator, to absorb-generator has the weak solution pipeline to be communicated with second absorber through the 3rd solution pump and second solution heat exchanger to be adjusted into absorption-generator and the weak solution pipeline to be arranged through the 3rd solution pump, the newly-increased solution heat exchanger and second solution heat exchanger are communicated with second absorber, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
58. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator through second solution heat exchanger in second generator is adjusted into second generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through second solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger, to absorb-generator has weak solution pipeline the 3rd solution pump and is communicated with second absorber through second solution heat exchanger and be adjusted into absorption-generator and the weak solution pipeline arranged through the 3rd solution pump, the newly-increased solution heat exchanger and second solution heat exchanger are communicated with second absorber, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator through first solution heat exchanger and second solution heat exchanger in first generator is adjusted into first generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through first solution heat exchanger and second solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger, to absorb-generator has weak solution pipeline the 3rd solution pump and is communicated with second absorber through second solution heat exchanger and be adjusted into absorption-generator and the weak solution pipeline arranged through the 3rd solution pump, the newly-increased solution heat exchanger and second solution heat exchanger are communicated with second absorber, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber.
59. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-6 item, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with absorption-generator through second solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through second solution heat exchanger and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
60. multiterminal heat supply the 3rd class absorption heat pump, be in the 7th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the weak solution pipeline to have the weak solution pipeline to be communicated with newly-increased absorber with dividing steam chest to be communicated with to be adjusted into second absorber second absorber through second solution heat exchanger and newly-increased solution heat exchanger through second solution heat exchanger and absorption-generator, newly-increased absorber also has the weak solution pipeline to be communicated with dividing steam chest through newly-increased solution heat exchanger and absorption-generator, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter or second condenser set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
61. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline through first solution pump, the newly-increased solution heat exchanger and first solution heat exchanger are communicated with first generator, with first absorber have heated medium pipeline and external communications be adjusted into first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
62. multiterminal heat supply the 3rd class absorption heat pump, be in the 10th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with first generator through first solution pump and first solution heat exchanger second absorber is adjusted into second absorber and has the weak solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline through first solution pump, the newly-increased solution heat exchanger and first solution heat exchanger are communicated with first generator, with first absorber have heated medium pipeline and external communications be adjusted into second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, or be adjusted into first condenser set up the cryogen liquid pipeline through newly-increased choke valve and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and first absorber after first absorber is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after first absorber is communicated with first absorber have the refrigerant vapour passage to be communicated with again with newly-increased absorber.
63. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-10 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, first generator had the refrigerant vapour passage to be communicated with first condenser to be adjusted into first generator has the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber has the weak solution pipeline to be communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has the refrigerant vapour passage to be communicated with first condenser, newly-increased generator drives thermal medium pipeline and external communications in addition, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first generator.
64. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-10 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased choke valve, first generator is set up the refrigerant vapour passage and is communicated with newly-increased absorber, newly-increased absorber has the weak solution pipeline to be communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has the refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has the cryogen liquid pipeline to be communicated with first condenser through newly-increased choke valve, newly-increased generator drives thermal medium pipeline and external communications in addition, newly-increased absorber and newly-increased condenser also have heated medium pipeline and external communications respectively, form two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first condenser and newly-increased absorber respectively by first generator.
65. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-10 item, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber has the weak solution pipeline to be communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased generator also has the refrigerant vapour passage to be communicated with first absorber, newly-increased generator drives thermal medium pipeline and external communications in addition, newly-increased absorber also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased generator.
66. multiterminal heat supply the 3rd class absorption heat pump, be in the 65th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased condenser and newly-increased choke valve, newly-increased generator is set up the refrigerant vapour passage and is communicated with newly-increased condenser, newly-increased condenser also has the cryogen liquid pipeline through the newly-increased choke valve and the first evaporimeter connected sum heated medium pipeline and external communications to be arranged respectively, forms by newly-increased generator and provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing the condenser and first absorber newly respectively.
67. multiterminal heat supply the 3rd class absorption heat pump, be at 5-6, in described multiterminal heat supply the 3rd class absorption heat pump of 8-9 item, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased generator, newly-increased absorption-evaporimeter, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, first evaporimeter is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, or first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber, newly-increased generator also has the refrigerant vapour passage and the first absorber connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber jointly by newly-increased generator and newly-increased absorption-evaporimeter.
68. multiterminal heat supply the 3rd class absorption heat pump, be the 7th, in 10 described multiterminal heat supply the 3rd class absorption heat pumps, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased absorption-evaporimeter, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter had the refrigerant vapour passage to be communicated with first absorber to be adjusted into first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with newly-increased generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, first evaporimeter or second condenser are set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing the cryogen liquid pump newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with first absorber again, newly-increased generator also has the refrigerant vapour passage and the first absorber connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber jointly by newly-increased generator and newly-increased absorption-evaporimeter; Wherein, when not having second evaporimeter, also can select to increase newly-increased choke valve and set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with by first condenser has the refrigerant vapour passage to be communicated with first absorber again.
69. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage economic benefits and social benefits of 11-23 item multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase generator newly has the refrigerant vapour passage to be communicated with first condenser to be adjusted into newly-increased generator to have the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber has the weak solution pipeline to be communicated with newly-increased second generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has the refrigerant vapour passage and the first condenser connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased absorber also has heated medium pipeline and external communications, and forming with the single-stage economic benefits and social benefits is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
70. multiterminal heat supply the 3rd class absorption heat pump, be in the 69th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve, to increase second generator newly has and drives thermal medium pipeline and external communications and be adjusted into first generator and set up the refrigerant vapour passage and is communicated with the back with newly-increased second generator and increases second generator newly and have cryogen liquid pipeline warp to increase the 3rd choke valve newly again to be communicated with first condenser, and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage economic benefits and social benefits.
71. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage economic benefits and social benefits of 11-23 item multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the 3rd choke valve, newly-increased generator is set up the refrigerant vapour passage and is communicated with newly-increased absorber, newly-increased absorber has the weak solution pipeline to be communicated with newly-increased second generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased second generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased second generator also has refrigerant vapour passage and newly-increased condenser connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased condenser also has the cryogen liquid pipeline to be communicated with first condenser through newly-increased the 3rd choke valve, newly-increased absorber and newly-increased condenser also have heated medium pipeline and external communications respectively, and forming with the single-stage economic benefits and social benefits is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
72. multiterminal heat supply the 3rd class absorption heat pump, be in the 71st described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 4th choke valve, to increase second generator newly has and drives thermal medium pipeline and external communications and be adjusted into first generator and set up the refrigerant vapour passage and is communicated with the back with newly-increased second generator and increases second generator newly and have cryogen liquid pipeline warp to increase the 4th choke valve newly again to be communicated with newly-increased condenser, and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage economic benefits and social benefits.
73. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage triple effect of 24-38 item multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase second generator newly has the refrigerant vapour passage to be communicated with first condenser to be adjusted into newly-increased second generator to have the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased the 3rd generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased the 3rd generator also has the refrigerant vapour passage and the first condenser connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased absorber also has heated medium pipeline and external communications, and forming with the single-stage triple effect is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
74. multiterminal heat supply the 3rd class absorption heat pump, be in the 73rd described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 4th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into newly-increased first generator and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 4th choke valve newly again to be communicated with first condenser, and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
75. multiterminal heat supply the 3rd class absorption heat pump, be in the 73rd described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 4th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into first generator and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 4th choke valve newly again to be communicated with first condenser, and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
76. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage triple effect of 21-31 item multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the 4th choke valve, newly-increased second generator is set up the refrigerant vapour passage and is communicated with newly-increased absorber, newly-increased absorber also has the weak solution pipeline to be communicated with newly-increased the 3rd generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased the 3rd generator also has refrigerant vapour passage and newly-increased condenser connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased condenser also has the cryogen liquid pipeline to be communicated with first condenser through newly-increased the 4th choke valve, newly-increased absorber and newly-increased condenser also have heated medium pipeline and external communications respectively, and forming with the single-stage triple effect is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
77. multiterminal heat supply the 3rd class absorption heat pump, be in the 76th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 5th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into newly-increased first generator and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 5th choke valve newly again to be communicated with newly-increased condenser, and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
78. multiterminal heat supply the 3rd class absorption heat pump, be in the 76th described multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 5th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into first generator and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 5th choke valve newly again to be communicated with newly-increased condenser, and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
79. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 11-38 item, increase newly-increased condenser and newly-increased the 4th choke valve, first generator is set up the refrigerant vapour passage and is communicated with newly-increased condenser, newly-increased condenser also has the cryogen liquid pipeline to be communicated with first condenser through newly-increased the 4th choke valve, newly-increased condenser also has heated medium pipeline and external communications, forms with multiterminal heat supply three class absorption heat pump of newly-increased condenser for additional high-temperature heat supply end.
80. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 24-38 item, increase newly-increased condenser and newly-increased the 4th choke valve, newly-increased first generator is set up the refrigerant vapour passage and is communicated with newly-increased condenser, newly-increased condenser also has the cryogen liquid pipeline to be communicated with first condenser through newly-increased the 4th choke valve, newly-increased condenser also has heated medium pipeline and external communications, forms with multiterminal heat supply three class absorption heat pump of newly-increased condenser for additional high-temperature heat supply end.
81. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of 5-62 item, increase the first flow control valve and second flow control valve, with first condenser have heated medium pipeline and external communications be adjusted into the outside have the heated medium pipeline be communicated with first condenser back first condenser have the heated medium pipeline to be communicated with second absorber with external communications with through second flow control valve through the first flow choke valve respectively again, having heated medium pipeline and external communications to be adjusted into first condenser second absorber has heated medium pipeline second absorber after the second flow choke valve and second absorber and external communications that heated medium pipeline and external communications are arranged again, forms adjustable type multiterminal heat supply the 3rd class absorption heat pump.
Description of drawings:
Fig. 1 loops back hot type absorption-generation systems the 1st kind of structure and schematic flow sheet according to single channel solution provided by the invention.
Fig. 2 loops back hot type absorption-generation systems the 1st kind of structure and schematic flow sheet according to two-way solution provided by the invention.
Fig. 3 loops back hot type absorption-generation systems the 2nd kind of structure and schematic flow sheet according to single channel solution provided by the invention.
Fig. 4 loops back hot type absorption-generation systems the 2nd kind of structure and schematic flow sheet according to two-way solution provided by the invention.
Fig. 5 loops back hot type absorption-generation systems the 3rd kind of structure and schematic flow sheet according to single channel solution provided by the invention.
Fig. 6 loops back hot type absorption-generation systems the 3rd kind of structure and schematic flow sheet according to two-way solution provided by the invention.
Fig. 7 is according to single-stage single-action multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 1st kind of structure and schematic flow sheet.
Fig. 8 is according to single-stage single-action multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 2nd kind of structure and schematic flow sheet.
Fig. 9 is according to single-stage single-action multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 3rd kind of structure and schematic flow sheet.
Figure 10 is according to single-stage single-action multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 4th kind of structure and schematic flow sheet.
Figure 11 is according to single-stage single-action multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 5th kind of structure and schematic flow sheet.
Figure 12 is according to single-stage single-action multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 6th kind of structure and schematic flow sheet.
Figure 13 is according to single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and schematic flow sheet.
Figure 14 is according to single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and schematic flow sheet.
Figure 15 is according to single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and schematic flow sheet.
Figure 16 invents single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump the 2nd kind of structure and the schematic flow sheet that provides according to this institute.
Figure 17 is according to single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and schematic flow sheet.
Figure 18 invents single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump the 4th kind of structure and the schematic flow sheet that provides according to this institute.
Figure 19 is according to single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and schematic flow sheet.
Figure 20 is according to single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 4th kind of structure and schematic flow sheet.
Figure 21 is according to single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 5th kind of structure and schematic flow sheet.
Figure 22 is according to single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump provided by the present invention the 6th kind of structure and schematic flow sheet.
Figure 23 is according to single-stage provided by the invention triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump structure and schematic flow sheet.
Figure 24 is according to single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 1st kind of structure and schematic flow sheet.
Figure 25 is according to single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 2nd kind of structure and schematic flow sheet.
Figure 26 is according to single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 3rd kind of structure and schematic flow sheet.
Figure 27 is according to single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump provided by the invention the 4th kind of structure and schematic flow sheet.
Figure 28 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of the invention provides, being provided to first absorber by absorption-evaporimeter refrigerant vapour.
Figure 29 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of the invention provides, being provided to first absorber by absorption-evaporimeter refrigerant vapour.
Figure 30 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet of the invention provides, being provided to first absorber by absorption-evaporimeter refrigerant vapour.
Figure 31 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 4th kind of structure and schematic flow sheet of the invention provides, being provided to first absorber by absorption-evaporimeter refrigerant vapour.
Figure 32 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 5th kind of structure and schematic flow sheet of the invention provides, being provided to first absorber by absorption-evaporimeter refrigerant vapour.
Figure 33 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 6th kind of structure and schematic flow sheet of the invention provides, being provided to first absorber by absorption-evaporimeter refrigerant vapour.
Figure 34 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 35 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 36 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 37 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 4th kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 38 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 5th kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 39 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 6th kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 40 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump the 7th kind of structure and schematic flow sheet of the invention provides, being provided to newly-increased absorber by first absorber refrigerant vapour.
Figure 41 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump structure and the schematic flow sheet that the invention provides, provided to newly-increased absorber by first generator refrigerant vapour.
Figure 42 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump structure and the schematic flow sheet that the invention provides, provided to first condenser and newly-increased absorber respectively by first generator refrigerant vapour.
Figure 43 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump structure and the schematic flow sheet that the invention provides, provided to first absorber by newly-increased generator refrigerant vapour.
Figure 44 is according to the invention provides, providing two-stage multiterminal heat supply the 3rd class absorption heat pump structure and the schematic flow sheet of refrigerant vapour to increasing the condenser and first absorber newly respectively by newly-increased generator.
Figure 45 is according to two-stage multiterminal heat supply the 3rd class absorption heat pump structure and the schematic flow sheet that the invention provides, provided to first absorber jointly by newly-increased absorption-evaporimeter and newly-increased generator refrigerant vapour.
Figure 46 is according to the invention provides, being two-stage multiterminal heat supply the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet of the first order with economic benefits and social benefits.
Figure 47 is according to the invention provides, being two-stage multiterminal heat supply the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet of the first order with economic benefits and social benefits.
Figure 48 be according to the invention provides, with single-stage economic benefits and social benefits multiterminal heat supply three class absorption heat pump structure and the schematic flow sheet of newly-increased condenser for additional high-temperature heat supply end.
Figure 49 is that foundation the invention provides, adjustable type single-stage single-action multiterminal heat supply the 3rd class absorption heat pump structure and schematic flow sheet.
Among the figure, 1-first absorber, 2-second absorber, 3-absorption-generator, 4-generator (rectifying column)/first generator, 5-second generator, 6-first solution pump, 7-second solution pump, 8-the 3rd solution pump, 9-first solution heat exchanger, 10-second solution heat exchanger, 11-the 3rd solution heat exchanger, 12-divides steam chest, 13-solution choke valve, 14-first condenser, 15-second condenser, 16-first evaporimeter, 17-second evaporimeter, 18-choke valve/first throttle valve, 19-cryogen liquid pump, 20-second choke valve; A-increases generator/newly-increased first generator newly, B-increases choke valve/newly-increased first throttle valve newly, C-increases solution heat exchanger/newly-increased first solution heat exchanger newly, D-increases second choke valve newly, E-increases solution pump/newly-increased first solution pump newly, F-increases second generator newly, and G-increases the 3rd choke valve newly, and H-increases second solution heat exchanger newly, I-increases second solution pump newly, J-increases absorption-evaporimeter newly, and K-increases the cryogen liquid pump newly, and L-increases absorber newly, M-increases condenser newly, N-increases the first flow control valve newly, and O-increases second flow control valve newly, and P-increases the 4th choke valve newly.
What need indicate is:
(1) among Fig. 1-4, second generator 5 and second absorber 2 are realized backheat; Among Fig. 5-6, the generator 4 and second absorber 2 are realized backheat.
(2) multiterminal heat supply is meant that the external heat supply parts of the 3rd class absorption heat pump have more than 3 or 3, mainly comprises first absorber 1, second condenser 14 and second absorber 2.
When (3) employing was the working media of representative with the ammonia spirit, this moment, generator was called rectifying column, and first rectifying column also will increase heated medium pipeline and external communications.
When (4) employing was the working media of representative with the ammonia spirit, the involved branch steam chest 12 of ammonia spirit increased cooling medium pipeline and external communications in case of necessity.
(5) Figure 1 shows that example, the concentrated solution of first generator 4 through first solution heat exchanger, 9 step-downs coolings, flow through absorptions-generator 3 heat absorptions and realize the part vaporization again, wherein first solution heat exchanger 6 has two effects---heat exchange between realization solution and concentrated solution carried out the throttling step-down; On the concentrated solution pipeline of first generator, 4 outlets, increase the solution choke valve in case of necessity.
(6) " parallel connection " in " single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump " is meant that the solution circulation was in parallel when multiterminal heat supply the 3rd class absorption heat pump was realized double-effect process; " single-stage triple effect in parallel " is also like this.
(7) " series connection " in " single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump " is meant that the solution circulation was series connection when multiterminal heat supply the 3rd class absorption heat pump was realized double-effect process; " single-stage serially connected three-effect " is also like this.
(8) be the address of having quoted in the first kind absorption heat pump such as " single-stage " in the terms such as " single-stage economic benefits and social benefits ", " economic benefits and social benefits " also are to have continued to use the angle that the high temperature driven thermal medium is had an effect in the first kind absorption heat pump to call.
(9) the main effect of absorption-generator 3 be to realize to flow through in it the solution heating and make its part vaporization, in the relatively low occasion of the initial temperature of some heated medium, absorptions-generator 3 can be born the external thermic load of part; But different with first absorber 1, second condenser 14 with second absorber, 2 these three heat supply ends, when bearing external thermic load, absorption-generator 3 can regard that replenishing of first absorber 1---this helps improving utilization rate of waste heat as.
The specific embodiment:
Describe the present invention in detail below in conjunction with accompanying drawing and example.When instantiation is explained, do not repeat to explain structure and flow process under the inessential situation.
Back-heating type absorption-generation systems shown in Figure 1 is achieved in that
1. on the structure, it mainly is made up of first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, the 3rd solution heat exchanger and branch steam chest; First absorber 1 has the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, second absorber 2 also has the weak solution pipeline to be communicated with absorption-generator 3 through second solution heat exchanger 10, absorption-generator 3 also has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9, first generator 4 also has the concentrated solution pipeline to be communicated with dividing steam chest 12 through first solution heat exchanger 9 and absorption-generator 3, divide steam chest 12 to also have the concentrated solution pipeline to be communicated with second generator 5 through second solution pump 7 and the 3rd solution heat exchanger 11, second generator 5 also has the concentrated solution pipeline to be communicated with first absorber 1 through the 3rd solution heat exchanger 11, first absorber 1 also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber 2 also has heated medium pipeline and external communications, second generator 5 also has refrigerant vapour passage and second absorber, 2 connected sums that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest 12 to also have refrigerant vapour passage and external communications, absorption-generator 3 also has refrigerant vapour passage and external communications, and first generator 4 also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications are arranged.
2. on the flow process, middle temperature refrigerant vapour (cryogen liquid absorbs steam or the afterheat steam that waste heat produces) from the outside enters first absorber 1, absorbed also heat release in heated medium by concentrated solution from second generator 5, the weak solution of first absorber 1 enters second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, absorption from the refrigerant vapour of second generator 5 and heat release in heated medium, the weak solution of second absorber 2 enters absorption-generator 3 through second solution heat exchanger 10, in the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 enters first generator 4 through first solution pump 6 and first solution heat exchanger 9 from the refrigerant vapour of outside and heat release in absorption; Driving the thermal medium heating enters the solution of first generator 4 and externally discharges refrigerant vapour, the concentrated solution of first generator 4 is lowered the temperature through 9 step-downs of first solution heat exchanger, flow through again and enter branch steam chest 12 after 3 heat absorptions of absorption-generator are vaporized, the solution that enters branch steam chest 12 carries out vapour, liquid separates and the external refrigerant vapour that discharges, divide the concentrated solution of steam chest 12 to enter second generator 5 through second solution pump 7 and the 3rd solution heat exchanger 11, the heating of driving thermal medium enters the solution release refrigerant vapour of second generator 5 and provides to second absorber 2, and the concentrated solution of second generator 5 enters first absorber 1 through the 3rd solution heat exchanger 11.
Back-heating type absorption-generation systems shown in Figure 2 is achieved in that
1. on the structure, it mainly is made up of first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, the 3rd solution heat exchanger and branch steam chest; First absorber 1 has the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, second absorber 2 also has the weak solution pipeline to be communicated with dividing steam chest 12 through second solution heat exchanger 10 and absorption-generator 3, divide steam chest 12 to also have the concentrated solution pipeline to be communicated with second generator 5 through second solution pump 7 and the 3rd solution heat exchanger 11, second generator 5 also has the concentrated solution pipeline to be communicated with first absorber 1 through the 3rd solution heat exchanger 11, absorption-generator 3 also has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9, first generator 4 also has the concentrated solution pipeline to be communicated with absorption-generator 3 through first solution heat exchanger 9, first absorber 1 also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber 2 also has heated medium pipeline and external communications, second generator 5 also has refrigerant vapour passage and second absorber, 2 connected sums that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest 12 to also have refrigerant vapour passage and external communications, absorption-generator 3 also has refrigerant vapour passage and external communications, and first generator 4 also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications are arranged.
2. on the flow process, middle temperature refrigerant vapour (cryogen liquid absorbs steam or the afterheat steam that waste heat produces) from the outside enters first absorber 1, absorbed also heat release in heated medium by concentrated solution from second generator 5, the weak solution of first absorber 1 enters second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, absorption from the refrigerant vapour of second generator 5 and heat release in heated medium, the weak solution of second absorber 2 is lowered the temperature through 10 step-downs of second solution heat exchanger, flow through again and enter branch steam chest 12 after 3 heat absorptions of absorption-generator are vaporized, the solution that enters branch steam chest 12 carries out vapour, liquid separates and the external refrigerant vapour that discharges, divide the concentrated solution of steam chest 12 to enter second generator 5 through second solution pump 7 and the 3rd solution heat exchanger 11, the heating of driving thermal medium enters the solution release refrigerant vapour of second generator 5 and provides to second absorber 2, and the concentrated solution of second generator 5 enters first absorber 1 through the 3rd solution heat exchanger 11; The concentrated solution of first generator 4 after first solution heat exchanger, 9 step-downs coolings, enter absorptions-generator 3, absorption from the refrigerant vapour of outside and heat release in the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 enters first generator 4 through first solution pump 6 and first solution heat exchanger 9, drives the thermal medium heating and enters the solution of first generator 4 and externally discharge refrigerant vapour.
Back-heating type absorption-generation systems shown in Figure 3 is achieved in that
1. on the structure, it mainly is made up of first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and branch steam chest; First absorber 1 has the weak solution pipeline to be communicated with absorption-generator 3, absorption-generator 3 also has the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, second absorber 2 also has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9, first generator 4 also has the concentrated solution pipeline to be communicated with second generator 5 through first solution heat exchanger 9, second generator 5 also has the concentrated solution pipeline to be communicated with dividing steam chest 12 through second solution heat exchanger 10 and absorption-generator 3, divide steam chest 12 to also have the concentrated solution pipeline to be communicated with first absorber 1 through second solution pump 7, first absorber 1 also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber 2 also has heated medium pipeline and external communications, second generator 5 also has refrigerant vapour passage and second absorber, 2 connected sums that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest 12 to also have refrigerant vapour passage and external communications, absorption-generator 3 also has refrigerant vapour passage and external communications, and first generator 4 also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications are arranged.
2. on the flow process, middle temperature refrigerant vapour (cryogen liquid absorbs steam or the afterheat steam that waste heat produces) from the outside enters first absorber 1, absorbed also heat release in heated medium by concentrated solution from minute steam chest 12, the weak solution of first absorber 1 enters absorption-generator 3, absorption from the refrigerant vapour of outside and heat release in the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 enters second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, absorption from the refrigerant vapour of second generator 5 and heat release in heated medium, the weak solution of second absorber 2 enters first generator 4 through first solution pump 6 and first solution heat exchanger 9, drives the thermal medium heating and enters the solution of first generator 4 and externally discharge refrigerant vapour; The concentrated solution of first generator 4 enters second generator 5 after first solution heat exchanger, 9 step-downs cooling, the heating of driving thermal medium enters the solution release refrigerant vapour of second generator 5 and provides to second absorber 2, the concentrated solution of second generator 5 enters branch steam chest 12 after the 3 heat absorption vaporizations of absorption-generator are lowered the temperature, flowed through in 10 step-downs of second solution heat exchanger, the solution that enters branch steam chest 12 carries out vapour, liquid separates and externally discharge refrigerant vapour, divides the concentrated solution of steam chest 12 to enter first absorber 1 through second solution pump 7.
Back-heating type absorption-generation systems shown in Figure 4 is achieved in that
1. on the structure, it mainly is made up of first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, branch steam chest and solution choke valve; First absorber 1 has the weak solution pipeline to be communicated with dividing steam chest 12 through solution choke valve 13 and absorption-generator 3, divide steam chest 12 to also have the concentrated solution pipeline to be communicated with first absorber 1 through second solution pump 7, absorption-generator 3 also has the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10, second absorber 2 also has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9, first generator 4 also has the concentrated solution pipeline to be communicated with second generator 5 through first solution heat exchanger 9, second generator 5 also has the concentrated solution pipeline to be communicated with absorption-generator 3 through second solution heat exchanger 10, first absorber 1 also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber 2 also has heated medium pipeline and external communications, second generator 5 also has refrigerant vapour passage and second absorber, 2 connected sums that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest 12 to also have refrigerant vapour passage and external communications, absorption-generator 3 also has refrigerant vapour passage and external communications, and first generator 4 also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications are arranged.
2. on the flow process, middle temperature refrigerant vapour (cryogen liquid absorbs steam or the afterheat steam that waste heat produces) from the outside enters first absorber 1, is absorbed also heat release in heated medium by the concentrated solution from minute steam chest 12, the weak solution of first absorber 1 is through the 13 throttling step-downs of solution choke valve, flow through and enter branch steam chest 12 after absorption-generator 3 heat absorption vaporization again, the solution that enters branch steam chest 12 carries out vapour, liquid separates and externally discharge refrigerant vapour, divides the concentrated solution of steam chest 12 to enter first absorber 1 through second solution pump 7; The weak solution of absorption-generator 3 enters second absorber 2, absorbs from the refrigerant vapour of second generator 5 and heat release in heated medium through the 3rd solution pump 8 and second solution heat exchanger 10, the weak solution of second absorber 2 enters first generator 4 through first solution pump 6 and first solution heat exchanger 9, drives the thermal medium heating and enters the solution of first generator 4 and externally discharge refrigerant vapour; The concentrated solution of first generator 4 enters second generator 5 after first solution heat exchanger, 9 step-downs cooling, drive solution that the thermal medium heating enters second generator 5 and discharge refrigerant vapour and provide to second absorber 2, the concentrated solution of second generator 5 after second solution heat exchanger, 10 step-downs cooling, enter absorptions-generator 3, absorption from the refrigerant vapour of outside and heat release in the solution of the absorption-generator 3 of flowing through.
Back-heating type absorption-generation systems shown in Figure 5 is achieved in that
In back-heating type absorption-generation systems shown in Figure 1, cancel second generator and the 3rd solution heat exchanger, second generator has the refrigerant vapour passage to be communicated with second absorber to change to first generator to increase the refrigerant vapour passage to be communicated with second absorber, divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger, second generator has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger to change to the branch steam chest and have the concentrated solution pipeline to be communicated with first absorber through second solution pump, form single channel solution and loop back hot type absorption-generation systems again.
Back-heating type absorption-generation systems shown in Figure 6 is achieved in that
In back-heating type absorption-generation systems shown in Figure 2, cancel second generator and the 3rd solution heat exchanger, second generator has the refrigerant vapour passage to be communicated with second absorber to change to first generator to increase the refrigerant vapour passage to be communicated with second absorber, divide steam chest to have the concentrated solution pipeline to be communicated with second generator through second solution pump and the 3rd solution heat exchanger, second generator has the concentrated solution pipeline to be communicated with first absorber through the 3rd solution heat exchanger to change to the branch steam chest and have the concentrated solution pipeline to be communicated with first absorber through second solution pump, form two-way solution and loop back hot type absorption-generation systems again.
Here it is to be noted:
1. shown in Figure 5 and shown in Figure 6, be respectively the result of cancellation second generator shown in Figure 1 and shown in Figure 2 and the 3rd solution heat exchanger; Simple in structure, the effect of backheat decreases.When cancelling second generator, same, back-heating type absorption-generation systems that backheat effect reduce simple in structure shown in Figure 3 and shown in Figure 4 to having.
2. in the back-heating type absorption-generation systems shown in Fig. 1-6, first generator 4 or second generator 5, second absorber 2 are realized backheat, and absorption-generator 3, branch steam chest 12 are formed the solution generation flow process that relies on the second class driving force.
Single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7 is achieved in that
1. on the structure, in back-heating type absorption-generation systems shown in Figure 1, absorption-generator 3 is set up heated medium pipeline and external communications, increase by first condenser again, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator 4 in first generator 4 has the refrigerant vapour passage to be communicated with first condenser 14, first condenser 14 also has the cryogen liquid pipeline to be communicated with first evaporimeter 16 through first throttle valve 18, first evaporimeter 16 also has the cryogen liquid pipeline to be communicated with second evaporimeter 17 through second choke valve 20, to divide steam chest 12 to have refrigerant vapour passage and external communications to be defined as branch steam chest 12 has the refrigerant vapour passage to be communicated with second condenser 15, second condenser 15 also has the cryogen liquid pipeline to be communicated with second evaporimeter 17 through cryogen liquid pump 19, having refrigerant vapour passage and external communications to be defined as first evaporimeter 16 first absorber 1 has the refrigerant vapour passage to be communicated with first absorber 1, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 17 has the refrigerant vapour passage to be communicated with absorption-generator 3, first condenser 14 also has heated medium pipeline and external communications, second condenser 15 also has cooling medium pipeline and external communications, first evaporimeter 16 and second evaporimeter 17 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 4 produces enters first condenser 14, heat release becomes cryogen liquid in heated medium, and the cryogen liquid of first condenser 14 enters first evaporimeter 16 after the 18 throttling step-downs of first throttle valve; The cryogen liquid that enters first evaporimeter 16 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to first absorber 1, and the second the tunnel enters second evaporimeter 17 after 20 throttlings of second choke valve; The refrigerant vapour that divides steam chest 12 to discharge enters second condenser 15, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of second condenser 15 enters second evaporimeter 17 through 19 pressurizations of cryogen liquid pump; The cryogen liquid that enters second evaporimeter 17 absorbs waste heat and becomes refrigerant vapour and formation single-stage single-action multiterminal heat supply the 3rd class absorption heat pump is provided to absorption-generator 3.
Single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 8 is achieved in that
1. on the structure, in back-heating type absorption-generation systems shown in Figure 2, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator 4 in first generator 4 has the refrigerant vapour passage to be communicated with first condenser 14, first condenser 14 also has the cryogen liquid pipeline to be communicated with second evaporimeter 17 through choke valve 18, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 17 has the refrigerant vapour passage to be communicated with absorption-generator 3, to divide steam chest 12 to have refrigerant vapour passage and external communications to be defined as branch steam chest 12 has the refrigerant vapour passage to be communicated with second condenser 15, second condenser 15 also has the cryogen liquid pipeline to be communicated with first evaporimeter 16 through cryogen liquid pump 19, having refrigerant vapour passage and external communications to be defined as first evaporimeter 16 first absorber 1 has the refrigerant vapour passage to be communicated with first absorber 1, first condenser 14 also has heated medium pipeline and external communications, second condenser 15 also has cooling medium pipeline and external communications, first evaporimeter 16 and second evaporimeter 17 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 4 produces enters first condenser 14, heat release becomes cryogen liquid in heated medium, and the cryogen liquid of first condenser 14 enters second evaporimeter 17 after choke valve 18 throttling step-downs, absorb waste heat becomes refrigerant vapour and provide to absorption-generator 3; The refrigerant vapour that divides steam chest 12 to discharge enters second condenser 15, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of second condenser 15 enters first evaporimeter 16, absorbs waste heat and become refrigerant vapour and provide to first absorber 1 through cryogen liquid pump 19, forms single-stage single-action multiterminal heat supply the 3rd class absorption heat pump.
Single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9 is achieved in that
1. on the structure, in back-heating type absorption-generation systems shown in Figure 3, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve, cryogen liquid pump and solution choke valve, first absorber 1 had the weak solution pipeline to be communicated with absorption-generator 3 to be adjusted into first absorber 1 has the weak solution pipeline to be communicated with absorption-generator 3 through solution choke valve 13, having refrigerant vapour passage and external communications to be defined as first generator 4 in first generator 4 has the refrigerant vapour passage to be communicated with first condenser 14, first condenser 14 also has the cryogen liquid pipeline to be communicated with first evaporimeter 16 through choke valve 18, to divide steam chest 12 to have refrigerant vapour passage and external communications to be defined as branch steam chest 12 has the refrigerant vapour passage to be communicated with second condenser 15, second condenser 15 also has the cryogen liquid pipeline to be communicated with second evaporimeter 17 through cryogen liquid pump 19, having refrigerant vapour passage and external communications to be defined as first evaporimeter 16 first absorber 1 has the refrigerant vapour passage to be communicated with first absorber 1, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 17 has the refrigerant vapour passage to be communicated with absorption-generator 3, first condenser 14 also has heated medium pipeline and external communications, second condenser 15 also has cooling medium pipeline and external communications, first evaporimeter 16 and second evaporimeter 17 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 4 produces enters first condenser 14, heat release becomes cryogen liquid in heated medium, and the cryogen liquid of first condenser 14 enters first evaporimeter 16 after choke valve 18 throttling step-downs, absorb waste heat becomes refrigerant vapour and provide to first absorber 1; The refrigerant vapour that divides steam chest 12 to discharge enters second condenser 15, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of second condenser 15 pressurizes and enters second evaporimeter 17, absorbs waste heat and becomes refrigerant vapour and formation single-stage single-action multiterminal heat supply the 3rd class absorption heat pump is provided to absorption-generator 3 through cryogen liquid pump 19.
Here it is to be noted, Figure 9 shows that representative, to loop back based on single channel solution in multiterminal heat supply the 3rd class absorption heat pump of hot type absorption-generation systems, also can select: increase by second choke valve 20 again, have the cryogen liquid pipeline to be communicated with second evaporimeter 17 through cryogen liquid pump 19 second condenser 15 and be adjusted into second condenser 15 and have the cryogen liquid pipeline to be communicated with first evaporimeter 16 through cryogen liquid pump 19, first evaporimeter 16 is set up the cryogen liquid pipeline and is communicated with second evaporimeter 17 through second choke valve 20.
Single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 10 is achieved in that
1. on the structure, in back-heating type absorption-generation systems shown in Figure 4, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator 4 in first generator 4 has the refrigerant vapour passage to be communicated with first condenser 14, first condenser 14 also has the cryogen liquid pipeline to be communicated with second evaporimeter 17 through choke valve 18, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 17 has the refrigerant vapour passage to be communicated with absorption-generator 3, to divide steam chest 12 to have refrigerant vapour passage and external communications to be defined as branch steam chest 12 has the refrigerant vapour passage to be communicated with second condenser 15, second condenser 15 also has the cryogen liquid pipeline to be communicated with first evaporimeter 16 through cryogen liquid pump 19, having refrigerant vapour passage and external communications to be defined as first evaporimeter 16 first absorber 1 has the refrigerant vapour passage to be communicated with first absorber 1, first condenser 14 also has heated medium pipeline and external communications, second condenser 15 also has cooling medium pipeline and external communications, first evaporimeter 16 and second evaporimeter 17 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 4 produces enters first condenser 14, heat release becomes cryogen liquid in heated medium, and the cryogen liquid of first condenser 14 enters second evaporimeter 17 after choke valve 18 throttling step-downs, absorb waste heat becomes refrigerant vapour and provide to absorption-generator 3; The refrigerant vapour that divides steam chest 12 to discharge enters second condenser 15, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of second condenser 15 enters first evaporimeter 16, absorbs waste heat and become refrigerant vapour and provide to first absorber 1 through cryogen liquid pump 19, forms single-stage single-action multiterminal heat supply the 3rd class absorption heat pump.
Single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 11 is achieved in that
1. on the structure, in back-heating type absorption-generation systems shown in Figure 5, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as generator 4 in generator 4 has the refrigerant vapour passage to be communicated with first condenser 14, first condenser 14 also has the cryogen liquid pipeline to be communicated with first evaporimeter 16 through first throttle valve 18, to divide steam chest 12 to have refrigerant vapour passage and external communications to be defined as branch steam chest 12 has the refrigerant vapour passage to be communicated with second condenser 15, second condenser 15 also has the cryogen liquid pipeline to be communicated with first evaporimeter 16 through cryogen liquid pump 19, first evaporimeter 16 also has the cryogen liquid pipeline to be communicated with second evaporimeter 17 through second choke valve 20, having refrigerant vapour passage and external communications to be defined as first evaporimeter 16 first absorber 1 has the refrigerant vapour passage to be communicated with first absorber 1, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as second evaporimeter 17 has the refrigerant vapour passage to be communicated with absorption-generator 3, first condenser 14 also has heated medium pipeline and external communications, second condenser 15 also has cooling medium pipeline and external communications, first evaporimeter 16 and second evaporimeter 17 also have surplus heat respectively medium pipeline and external communications.
2. on the flow process, the part refrigerant vapour that generator 4 produces enters first condenser 14, heat release becomes cryogen liquid in heated medium, and the cryogen liquid of first condenser 14 enters first evaporimeter 16 after 18 throttlings of first throttle valve; The refrigerant vapour that divides steam chest 12 to discharge enters second condenser 15, heat release becomes cryogen liquid in cooling medium, and the cryogen liquid of second condenser 15 enters first evaporimeter 16 after 19 pressurizations of cryogen liquid pump; The cryogen liquid that enters first evaporimeter 16 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to first absorber 1, the second the tunnel after 20 throttlings of second choke valve, enter second evaporimeter 17, absorb waste heat and become refrigerant vapour and formation single-stage single-action multiterminal heat supply the 3rd class absorption heat pump is provided to absorptions-generator 3.
Single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 12 is achieved in that
1. on the structure, in back-heating type absorption-generation systems shown in Figure 6, increase by first condenser, second condenser, evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as generator 4 in generator 4 has the refrigerant vapour passage to be communicated with first condenser 14, first condenser 14 also has the cryogen liquid pipeline to be communicated with evaporimeter 16 through choke valve 18, to divide steam chest 12 to have refrigerant vapour passage and external communications to be defined as branch steam chest 12 has the refrigerant vapour passage to be communicated with second condenser 15, second condenser 15 also has the cryogen liquid pipeline to be communicated with evaporimeter 16 through cryogen liquid pump 19, having refrigerant vapour passage and external communications to be defined as evaporimeter 16 first absorber 1 has the refrigerant vapour passage to be communicated with first absorber 1, to absorb-generator 3 has refrigerant vapour passage and external communications to be defined as evaporimeter 16 has the refrigerant vapour passage to be communicated with absorption-generator 3, first condenser 14 also has heated medium pipeline and external communications, second condenser 15 also has cooling medium pipeline and external communications, evaporimeter 16 also have surplus heat medium pipeline and external communications.
2. on the flow process, the part refrigerant vapour that generator 4 produces enters first condenser 14, heat release becomes cryogen liquid in heated medium, the cryogen liquid of first condenser 14 enters evaporimeter 16 after choke valve 18 throttlings, the refrigerant vapour that divides steam chest 12 to discharge enters second condenser 15, heat release becomes cryogen liquid in cooling medium, the cryogen liquid of second condenser 15 enters evaporimeter 16 after 19 pressurizations of cryogen liquid pump, the cryogen liquid that enters evaporimeter 16 absorbs waste heat and becomes refrigerant vapour and formation single-stage single-action multiterminal heat supply the 3rd class absorption heat pump is provided to first absorber 1 and absorption-generator 3 respectively.
Single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 13 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump 6 is set up the weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to converge through newly-increased solution heat exchanger C and the concentrated solution pipeline of first generator 4 after first solution heat exchanger 9, be communicated with dividing steam chest 12 through absorption-generator 3 again, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B again, increases generator A newly and also have the refrigerant vapour passage to be communicated with first condenser 14.
2. on the flow process, the refrigerant vapour that first generator 4 discharges provides to drive thermal medium as it to newly-increased generator A, a part of weak solution of absorption-generator 3 enters newly-increased generator A through first solution pump 6 and newly-increased solution heat exchanger C, from the refrigerant vapour of the first generator 4 newly-increased generator A that flows through, heating enters the solution release refrigerant vapour of newly-increased generator A and provides to first condenser 14, the concentrated solution of the newly-increased generator A absorption-generator 3 of after newly-increased solution heat exchanger C, flowing through again, enter branch steam chest 12 after the heat absorbing part vaporization, flowing through enters first condenser 14 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid again, forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
Single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 14 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 13, increase the newly-increased second choke valve D, second generator 5 being had drives thermal medium pipeline and external communications and be adjusted into first generator 4 and set up the refrigerant vapour passage and is communicated with back second generator 5 with second generator 5 and has the cryogen liquid pipeline to be communicated with first condenser 14 again through increasing the second choke valve D newly---a part of refrigerant vapour of first generator, 4 releases is as the driving thermal medium of second generator 5, formation single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
Single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 15 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 8, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator 3 through first solution heat exchanger 9 in first generator 4 is adjusted into first generator 4 and has the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with absorption-generator 3 through first solution heat exchanger 9, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 to be adjusted into absorption-generator 3 and the weak solution pipeline to be arranged through first solution pump 6, first solution heat exchanger 9 and newly-increased solution heat exchanger C are communicated with first generator 4, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B again---and the refrigerant vapour that first generator produces increases generator A newly and also has the refrigerant vapour passage to be communicated with first condenser 14 as the driving thermal medium that increases generator newly.
2. on the flow process, the weak solution of absorption-generator 3 is through first solution pump 6, first solution heat exchanger 9 and newly-increased solution heat exchanger C enter first generator 4, the concentrated solution of first generator 4 enters newly-increased generator A through newly-increased solution heat exchanger C, the refrigerant vapour that first generator 4 discharges is flowed through and is increased generator A newly, heating enters its interior solution release refrigerant vapour and provides to first condenser 14, the concentrated solution of newly-increased generator A enters absorption-generator 3 through first solution heat exchanger 9, flowing through enters first condenser 14 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid again, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
Single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 16 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 15, increase the newly-increased second choke valve D, second generator 5 there is drive thermal medium pipeline and external communications and be adjusted into first generator 4 and set up the refrigerant vapour passage and is communicated with back second generator 5 with second generator 5 and has the cryogen liquid pipeline to be communicated with first condenser 14 again formation single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump of connecting through increasing the second choke valve D newly.
Single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 17 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 second absorber 2 is adjusted into second absorber 2 and has the weak solution pipeline to be communicated with newly-increased generator A through first solution pump 6 and first solution heat exchanger 9, newly-increased generator A also has the concentrated solution pipeline to be communicated with first generator 4 through newly-increased solution pump E and newly-increased solution heat exchanger C, having the concentrated solution pipeline to be communicated with second generator 5 through first solution heat exchanger 9 in first generator 4 is adjusted into first generator 4 and has the concentrated solution pipeline to be communicated with second generator 5 through the newly-increased solution heat exchanger C and first solution heat exchanger 9, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B again---and the refrigerant vapour that first generator produces increases generator A newly and also has the refrigerant vapour passage to be communicated with first condenser 14 as the driving thermal medium that increases generator newly.
2. on the flow process, the weak solution of second absorber 2 enters newly-increased generator A through first solution pump 6 and first solution heat exchanger 9, the refrigerant vapour that first generator 4 discharges is flowed through and is increased generator A newly, heating enters its interior solution release refrigerant vapour and provides to first condenser 14, the concentrated solution of newly-increased generator A enters first generator 4 through newly-increased solution pump E and newly-increased solution heat exchanger C, the concentrated solution of first generator 4 enters second generator 5 through the newly-increased solution heat exchanger C and first solution heat exchanger 9, flowing through enters first condenser 14 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid again, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
Single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 180 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 17, having the weak solution pipeline to be communicated with newly-increased generator A through first solution pump 6 and first solution heat exchanger 9 second absorber 2 is adjusted into second absorber 2 and has the weak solution pipeline to be communicated with first generator 4 and newly-increased generator A respectively after first solution pump 6 and first solution heat exchanger 9, increase the newly-increased second choke valve D again, second generator 5 there is drive thermal medium pipeline and external communications and be adjusted into first generator 4 and set up the refrigerant vapour passage and is communicated with back second generator 5 with second generator 5 and has the cryogen liquid pipeline to be communicated with first condenser 14 again formation single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump of connecting through increasing the second choke valve D newly.
Here it is to be noted that the economic benefits and social benefits among Figure 18 are referred to as the connection in series-parallel economic benefits and social benefits again; Involved in the present invention to the series connection double-effect process all can adopt the similar techniques measure to form corresponding connection in series-parallel double-effect process.
In addition, when effect is little, first solution heat exchanger 9 among Figure 17-18 can be cancelled, and second absorber 2 has the weak solution pipeline to be communicated with newly-increased absorber A through first solution pump 6, and first generator 4 has the concentrated solution pipeline to be communicated with second generator 5 through newly-increased solution heat exchanger C.
Single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 19 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 11, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump 6 is set up the weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to converge through newly-increased solution heat exchanger C and the concentrated solution pipeline of first generator 4 after first solution heat exchanger 9, be communicated with dividing steam chest 12 through absorption-generator 3 again, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B again---and the refrigerant vapour that first generator produces increases generator A newly and also has the refrigerant vapour passage to be communicated with first condenser 14 as the driving thermal medium that increases generator newly.
2. on the flow process, a part of weak solution of absorption-generator 3 enters newly-increased generator A through first solution pump 6 and newly-increased solution heat exchanger C, from the refrigerant vapour of the first generator 4 newly-increased generator A that flows through, heating enters the solution release refrigerant vapour of newly-increased generator A and provides to first condenser 14, the concentrated solution of the newly-increased generator A absorption-generator 3 of after newly-increased solution heat exchanger C, flowing through again, enter branch steam chest 12 after the heat absorbing part vaporization, flowing through enters first condenser 14 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid again, forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
Single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 20 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 19, there is the refrigerant vapour passage to be communicated with to be adjusted into the newly-increased first generator A to set up the refrigerant vapour passage in first generator 4 and is communicated with, formation single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump with second absorber 2 with second absorber 2.
Single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 21 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 11, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the refrigerant vapour passage to be communicated with second absorber 2 to be adjusted into newly-increased generator A to set up the refrigerant vapour passage in first generator 4 is communicated with second absorber 2, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 to be adjusted into absorption-generator 3 and the weak solution pipeline to be arranged through first solution pump 6, first solution heat exchanger 9 and newly-increased solution heat exchanger C are communicated with first generator 4, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator A with dividing steam chest 12 to be communicated with to be adjusted into first generator 4 in first generator 4 through increasing solution heat exchanger C newly through first solution heat exchanger 9 and absorption-generator 3, newly-increased generator A also has the concentrated solution pipeline to be communicated with dividing steam chest 12 through first solution heat exchanger 9 and absorption-generator 3, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B again---and the refrigerant vapour that first generator produces increases generator A newly and also has the refrigerant vapour passage to be communicated with first condenser 14 as the driving thermal medium that increases generator newly.
2. on the flow process, the weak solution of absorption-generator 3 is through first solution pump 6, first solution heat exchanger 9 and newly-increased solution heat exchanger C enter generator 4, the refrigerant vapour that generator 4 discharges provides to drive thermal medium as it to newly-increased generator A, the concentrated solution of generator 4 enters newly-increased generator A through newly-increased solution heat exchanger C, from the refrigerant vapour of the generator 4 newly-increased generator A that flows through, heating enters the solution release refrigerant vapour in it and provides to first condenser 14 and second absorber 2 respectively, the concentrated solution of newly-increased generator A is lowered the temperature through 9 step-downs of first solution heat exchanger, enter branch steam chest 12 after absorption-generator 3 heat absorbing parts of flowing through again vaporization, flowing through enters first condenser 14 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid again, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
Single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 22 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 12, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the refrigerant vapour passage to be communicated with second absorber 2 to be adjusted into newly-increased generator A to set up the refrigerant vapour passage in first generator 4 is communicated with second absorber 2, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with newly-increased generator A through first solution pump 6 and first solution heat exchanger 9, newly-increased generator A also has the concentrated solution pipeline to be communicated with first generator 4 through newly-increased solution pump E and newly-increased solution heat exchanger C, having the concentrated solution pipeline to be communicated with absorption-generator 3 through first solution heat exchanger 9 in first generator 4 is adjusted into first generator 4 and has the concentrated solution pipeline to be communicated with absorption-generator 3 through the newly-increased solution heat exchanger C and first solution heat exchanger 9, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have the refrigerant vapour passage to be communicated with the newly-increased generator A in back with newly-increased generator A in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B again---and the refrigerant vapour that first generator produces increases generator A newly and also has the refrigerant vapour passage to be communicated with first condenser 14 as the driving thermal medium that increases generator newly.
2. on the flow process, the weak solution of absorption-generator 3 enters newly-increased generator A through first solution pump 6 and first solution heat exchanger 9, the refrigerant vapour that generator 4 discharges provides to drive thermal medium as it to newly-increased generator A, from the refrigerant vapour of the generator 4 newly-increased generator A that flows through, heating enters the solution release refrigerant vapour in it and provides to first condenser 14 and second absorber 2 respectively, the concentrated solution of newly-increased generator A enters generator 4 through newly-increased solution pump E and newly-increased solution heat exchanger C, the concentrated solution of generator 4 enters absorption-generator 3 through the newly-increased solution heat exchanger C and first solution heat exchanger 9, flowing through enters first condenser 14 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A becomes cryogen liquid again, forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
Single-stage shown in Figure 23 triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 10, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump 6 is set up the weak solution pipeline and is communicated with the newly-increased second generator F through the newly-increased second solution heat exchanger H with the newly-increased first generator A connected sum through the newly-increased first solution heat exchanger C respectively, the newly-increased first generator A also has the concentrated solution pipeline to be communicated with second generator 5 through the newly-increased first solution heat exchanger C, the newly-increased second generator F also has the concentrated solution pipeline to be communicated with second generator 5 through the newly-increased second solution heat exchanger H, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have refrigerant vapour passage and the newly-increased first generator A to be communicated with the newly-increased first generator A in back in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased first throttle valve B again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases the first generator A newly, the newly-increased first generator A also has the refrigerant vapour passage to be communicated with the newly-increased second generator F in back with the newly-increased second generator F has the newly-increased second choke valve D of cryogen liquid pipeline warp to be communicated with first condenser 14 again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, and the newly-increased second generator F also has the refrigerant vapour passage to be communicated with first condenser 14.
2. on the flow process, the part weak solution of second absorber 2 enters the newly-increased first generator A through first solution pump 6 and the newly-increased first solution heat exchanger C, enter solution in it and discharge refrigerant vapour and provide from the flow through newly-increased first generator A, heating of the refrigerant vapour of first generator 4 to the newly-increased second generator F, the concentrated solution of the newly-increased first generator A enters second generator 5 through the newly-increased first solution heat exchanger C, and the refrigerant vapour heat release of the newly-increased first generator A that flows through becomes cryogen liquid, enters first condenser 14 through newly-increased first throttle valve B again; The part weak solution of second absorber 2 enters the newly-increased second generator F through first solution pump 6 and the newly-increased second solution heat exchanger H, from the refrigerant vapour of the newly-increased first generator A newly-increased second generator F that flows through, heating enters its interior solution release refrigerant vapour and provides to first condenser 14, the concentrated solution of the newly-increased second generator F enters second generator 5 through the newly-increased second solution heat exchanger H, the refrigerant vapour heat release that increases the second generator F newly of flowing through becomes cryogen liquid, enter first condenser 14 through the newly-increased second choke valve D again, form single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
Single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 24 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 10, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator 5 through first solution heat exchanger 9 in first generator 4 is adjusted into first generator 4 and has the concentrated solution pipeline to be communicated with the newly-increased first generator A through first solution heat exchanger 9, the newly-increased first generator A also has the concentrated solution pipeline to be communicated with the newly-increased second generator F through the newly-increased first solution heat exchanger C, the newly-increased second generator F also has the concentrated solution pipeline to be communicated with second generator 5 through the newly-increased second solution heat exchanger H, having the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 second absorber 2 is adjusted into second absorber 2 and the weak solution pipeline is arranged through first solution pump 6, the newly-increased second solution heat exchanger H, the newly-increased first solution heat exchanger C and first solution heat exchanger 9 are communicated with first generator 4, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have refrigerant vapour passage and the newly-increased first generator A to be communicated with the newly-increased first generator A in back in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased first throttle valve B again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases the first generator A newly, the newly-increased first generator A also has the refrigerant vapour passage to be communicated with the newly-increased second generator F in back with the newly-increased second generator F has the newly-increased second choke valve D of cryogen liquid pipeline warp to be communicated with first condenser 14 again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, and the newly-increased second generator F also has the refrigerant vapour passage to be communicated with first condenser 14.
2. on the flow process, the weak solution of second absorber 2 is through first solution pump 6, the newly-increased second solution heat exchanger H, the newly-increased first solution heat exchanger C and first solution heat exchanger 9 enter first generator 4, the refrigerant vapour that first generator 4 produces provides to the newly-increased first generator A, the concentrated solution of first generator 4 enters newly-increased generator A through first solution heat exchanger 9, from the refrigerant vapour of the first generator 4 newly-increased first generator A that flows through, heating enters its interior solution release refrigerant vapour and provides to the newly-increased second generator F, the concentrated solution of the newly-increased first generator A enters the newly-increased second generator F through the newly-increased first solution heat exchanger C, and the refrigerant vapour heat release of the newly-increased first generator A that flows through becomes cryogen liquid, enter first condenser 14 through newly-increased first throttle valve B again; Enter solution in it and discharge refrigerant vapour and provide from the flow through newly-increased second generator F, heating of the refrigerant vapour of the newly-increased first generator A to first condenser 14, the concentrated solution of the newly-increased second generator F enters second generator 5 through the newly-increased second solution heat exchanger H, the refrigerant vapour heat release that increases the second generator F newly of flowing through becomes cryogen liquid, enters first condenser 14 through the newly-increased second choke valve D again, forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
Single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 25 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 24, increase newly-increased the 3rd choke valve G, second generator 5 had drive thermal medium pipeline and external communications and be adjusted into the newly-increased first generator A and set up the refrigerant vapour passage and is communicated with back second generator 5 with second generator 5 and has cryogen liquid pipeline warp to increase the 3rd choke valve G newly again to be communicated with formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with first condenser 14.
Single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 26 is achieved in that
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 10, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 second absorber 2 is adjusted into second absorber 2 and has the weak solution pipeline to be communicated with the newly-increased second generator F through first solution pump 6 and first solution heat exchanger 9, the newly-increased second generator F also has the concentrated solution pipeline to be communicated with the newly-increased first generator A through newly-increased second solution pump I and the newly-increased second solution heat exchanger H, the newly-increased first generator A also has the concentrated solution pipeline to be communicated with first generator 4 through newly-increased first solution pump E and the newly-increased first solution heat exchanger C, having the concentrated solution pipeline to be communicated with second generator 5 through first solution heat exchanger 9 in first generator 4 is adjusted into first generator 4 and the concentrated solution pipeline is arranged through the newly-increased first solution heat exchanger C, the newly-increased second solution heat exchanger H and first solution heat exchanger 9 are communicated with second generator 5, having the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 to have refrigerant vapour passage and the newly-increased first generator A to be communicated with the newly-increased first generator A in back in first generator 4 has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased first throttle valve B again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases the first generator A newly, the newly-increased first generator A also has the refrigerant vapour passage to be communicated with the newly-increased second generator F in back with the newly-increased second generator F has the newly-increased second choke valve D of cryogen liquid pipeline warp to be communicated with first condenser 14 again---and the refrigerant vapour that newly-increased first generator produces is as the driving thermal medium that increases second generator newly, and the newly-increased second generator F also has the refrigerant vapour passage to be communicated with first condenser 14.
2. on the flow process, the weak solution of second absorber 2 enters the newly-increased second generator F through first solution pump 6 and first solution heat exchanger 9, enter solution in it and discharge refrigerant vapour and provide from the flow through newly-increased second generator F, heating of the refrigerant vapour of the newly-increased first generator A to first condenser 14, the concentrated solution of the newly-increased second generator F enters the newly-increased first generator A through newly-increased second solution pump I and the newly-increased second solution heat exchanger H, and the refrigerant vapour heat release of the second generator F that flows through enters first condenser 14 through the newly-increased second choke valve D after becoming cryogen liquid again; From the refrigerant vapour of the first generator 4 newly-increased first generator A that flows through, heating enters its interior solution release refrigerant vapour and provides to the newly-increased second generator F, the concentrated solution of the newly-increased first generator A enters first generator 4 through newly-increased first solution pump E and the newly-increased first solution heat exchanger C, flow through and enter first condenser 14 through newly-increased first throttle valve B again after the refrigerant vapour heat release of the newly-increased first generator A becomes cryogen liquid, the concentrated solution of first generator 4 is through the newly-increased first solution heat exchanger C, the newly-increased second solution heat exchanger H and first solution heat exchanger 9 enter second generator 5, form single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
Single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump shown in Figure 27 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 26, increase newly-increased the 3rd choke valve G, second generator 5 had drive thermal medium pipeline and external communications and be adjusted into first generator 4 and set up the refrigerant vapour passage and is communicated with back second generator 5 with second generator 5 and has cryogen liquid pipeline warp to increase the 3rd choke valve G newly again to be communicated with formation single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump with first condenser 14.
Among Figure 26-27, optional first solution heat exchanger 9 that disappears of selecting; At this moment, second absorber 2 has the weak solution pipeline to be communicated with the newly-increased second generator F through first solution pump 6, and first generator 4 has the concentrated solution pipeline to be communicated with second generator 5 through newly-increased first solution heat exchanger C and the newly-increased second solution heat exchanger H.
Shown in Figure 28, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by absorption-evaporimeter to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel the cryogen liquid pipeline that first evaporimeter 16 is communicated with second evaporimeter 17 through second choke valve 20, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10 first absorber 1 is adjusted into first absorber 1 and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter J through newly-increased solution heat exchanger C, newly-increased absorption-evaporimeter J has the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10 again, to divide steam chest 12 to have the concentrated solution pipeline to be communicated with second generator 5 through second solution pump 7 and the 3rd solution heat exchanger 11 is adjusted into branch steam chest 12 and the concentrated solution pipeline is arranged through second solution pump 7, newly-increased second solution heat exchanger C and the 3rd solution heat exchanger 11 are communicated with second generator 5, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, first evaporimeter 16 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump K with increase absorption-evaporimeter J newly after newly-increased absorption-evaporimeter J is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber 1.
2. on the flow process, the cryogen liquid that enters first evaporimeter 16 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to newly-increased absorptions-evaporimeter J, and the second the tunnel increases absorption-evaporimeter J newly, absorbs heat into refrigerant vapour and provide to first absorber 1 through increasing newly to flow through after cryogen liquid pump K pressurizes; Refrigerant vapour and heat release that the weak solution of first absorber 1 enters through newly-increased solution heat exchanger C and increases absorption-evaporimeter J newly, absorbs from first evaporimeter 16 increase the cryogen liquid of absorption-evaporimeter J newly in flowing through, and the weak solution of newly-increased absorption-evaporimeter J enters second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10; Divide the concentrated solution of steam chest 12 to enter second generator 5 through newly-increased solution heat exchanger C and the 3rd solution heat exchanger 11, the concentrated solution of second generator 5 enters first absorber 1, absorbs from the refrigerant vapour of newly-increased absorptions-evaporimeter J and heat release in heated medium through the 3rd solution heat exchanger 11, and formation is provided two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to first absorber by absorption-evaporimeter.
Shown in Figure 29, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by absorption-evaporimeter to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel the cryogen liquid pipeline that first evaporimeter 16 is communicated with second evaporimeter 17 through second choke valve 20, increase newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the concentrated solution pipeline to be communicated with first absorber 1 through the 3rd solution heat exchanger 11 in second generator 5 is adjusted into second generator 5 and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter J through the 3rd solution heat exchanger 11, newly-increased absorption-evaporimeter J has the weak solution pipeline to be communicated with first absorber 1 through newly-increased solution pump E and newly-increased solution heat exchanger C again, having the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10 first absorber 1 is adjusted into first absorber 1 and the weak solution pipeline is arranged through newly-increased solution heat exchanger C, the 3rd solution pump 8 and second solution heat exchanger 10 are communicated with second absorber 2, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, first condenser 14 set up the cryogen liquid pipeline through newly-increased choke valve B with increase absorption-evaporimeter J newly after newly-increased absorption-evaporimeter J is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber 1.
2. on the flow process, the concentrated solution of second generator 5 enters newly-increased absorption-evaporimeter J through the 3rd solution heat exchanger 11, absorption increases the cryogen liquid of absorption-evaporimeter J newly from the refrigerant vapour and the heat release of first evaporimeter 16 in flowing through, the weak solution of newly-increased absorption-evaporimeter J enters first absorber 1 through newly-increased solution pump E and newly-increased solution heat exchanger C, the weak solution of first absorber 1 is through newly-increased solution heat exchanger C, the 3rd solution pump 8 and second solution heat exchanger 10 enter second absorber 2, the part cryogen liquid of first condenser 14 is flowed through after newly-increased choke valve B throttling again and is increased absorption-evaporimeter J newly, absorb heat into refrigerant vapour and provide, form two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by absorption-evaporimeter to first absorber 1.
Shown in Figure 30, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by absorption-evaporimeter to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with absorption-generator 3 through solution choke valve 13 first absorber 1 is adjusted into first absorber 1 and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter J through newly-increased solution heat exchanger C, newly-increased absorption-evaporimeter J has the weak solution pipeline to be communicated with absorption-generator 3 through solution choke valve 13 again, to divide steam chest 12 to have the concentrated solution pipeline to be communicated with first absorber 1 through second solution pump 7 is adjusted into branch steam chest 12 and has the concentrated solution pipeline to be communicated with first absorber 1 through second solution pump 7 and newly-increased solution heat exchanger C, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, first evaporimeter 16 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump K with increase absorption-evaporimeter J newly after newly-increased absorption-evaporimeter J is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber 1.
2. on the flow process, the concentrated solution of dividing steam chest 12 enters first absorber 1, absorbs from the refrigerant vapour of newly-increased absorption-evaporimeter J and heat release in heated medium through second solution pump 7 and newly-increased solution heat exchanger C, refrigerant vapour and heat release that the weak solution of first absorber 1 enters through newly-increased solution heat exchanger C and increases absorption-evaporimeter J newly, absorbs from first evaporimeter 16 increase the cryogen liquid of absorption-evaporimeter J newly in flowing through, and the weak solution of newly-increased absorption-evaporimeter J enters absorption-generator 3 through solution choke valve 13; The cryogen liquid that enters first evaporimeter 16 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to newly-increased absorption-evaporimeter J, the second the tunnel after newly-increased cryogen liquid pump K pressurization, flow through again newly-increased absorptions-evaporimeter J, absorb heat into refrigerant vapour and provide to first absorber 1, formation is provided two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to first absorber by absorption-evaporimeter.
Shown in Figure 31, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by absorption-evaporimeter to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, cancellation solution choke valve 13, increase newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with absorption-generator 3 through solution choke valve 13 first absorber 1 is adjusted into first absorber 1 and has the weak solution pipeline to be communicated with absorption-generator 3 through newly-increased solution heat exchanger C, to divide steam chest 12 to have the concentrated solution pipeline to be communicated with first absorber 1 through second solution pump 7 is adjusted into branch steam chest 12 and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter J through second solution pump 7, newly-increased absorption-evaporimeter J has the weak solution pipeline to be communicated with first absorber 1 through newly-increased solution pump E and newly-increased solution heat exchanger C again, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, first condenser 14 set up the cryogen liquid pipeline through newly-increased choke valve B with increase absorption-evaporimeter J newly after newly-increased absorption-evaporimeter J is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber 1.
2. on the flow process, refrigerant vapour and heat release that the concentrated solution of branch steam chest 12 enters through second solution pump 7 and increases absorption-evaporimeter J newly, absorbs from first evaporimeter 16 increase the cryogen liquid of absorption-evaporimeter J newly in flowing through, the weak solution of newly-increased absorptions-evaporimeter J enters first absorber 1, absorbs from the refrigerant vapour of newly-increased absorptions-evaporimeter J and heat release in heated medium through newly-increased solution pump E and newly-increased solution heat exchanger C, and the weak solution of first absorber 1 warp increases solution heat exchanger C newly and enters absorption-generator 3; The part cryogen liquid of first condenser 14 after newly-increased choke valve B throttling, flow through again newly-increased absorptions-evaporimeter J, absorb heat into refrigerant vapour and provide to first absorber 1, formation is provided two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to first absorber by absorption-evaporimeter.
Shown in Figure 32, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by absorption-evaporimeter to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 10, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, there is the weak solution pipeline to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter J with dividing steam chest 12 to be communicated with to be adjusted into first absorber 1 first absorber 1 through increasing solution heat exchanger C newly through solution choke valve 13 and absorption-generator 3, newly-increased absorption-evaporimeter J has the weak solution pipeline to be communicated with dividing steam chest 12 through solution choke valve 13 and absorption-generator 3 again, to divide steam chest 12 to have the concentrated solution pipeline to be communicated with to be adjusted into branch steam chest 12 to have the concentrated solution pipeline to be communicated with first absorber 1 through newly-increased solution heat exchanger C with first absorber 1, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, and first evaporimeter 16 is set up cryogen liquid pump K and is communicated with the newly-increased absorption-evaporimeter J in back with newly-increased absorption-evaporimeter J and has the refrigerant vapour passage to be communicated with first absorber 1 again.
2. on the flow process, the concentrated solution of dividing steam chest 12 enters first absorber 1, absorbs from the refrigerant vapour of newly-increased absorption-evaporimeter J and heat release in heated medium through second solution pump 7 and newly-increased solution heat exchanger C, refrigerant vapour and heat release that the weak solution of first absorber 1 enters through newly-increased solution heat exchanger C and increases absorption-evaporimeter J newly, absorbs from first evaporimeter 16 increase the cryogen liquid of absorption-evaporimeter J newly in flowing through, and the weak solution of newly-increased absorption-evaporimeter J enters branch steam chest 12 through solution choke valve 13 and absorption-generator 3; The cryogen liquid that enters first evaporimeter 16 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to newly-increased absorption-evaporimeter J, the second the tunnel after newly-increased cryogen liquid pump K pressurization, flow through again newly-increased absorptions-evaporimeter J, absorb heat into refrigerant vapour and provide to first absorber 1, formation is provided two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to first absorber by absorption-evaporimeter.
Shown in Figure 33, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by absorption-evaporimeter to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 10, increase newly-increased absorption-evaporimeter, newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest 12 to have the concentrated solution pipeline to be communicated with first absorber 1 to be adjusted into branch steam chest 12 has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter J, newly-increased absorption-evaporimeter J has the weak solution pipeline to be communicated with first absorber 1 through newly-increased solution pump E and newly-increased solution heat exchanger C again, cancellation solution choke valve 13, there is the weak solution pipeline to have the weak solution pipeline to be communicated with branch steam chest 12 with dividing steam chest 12 to be communicated with to be adjusted into first absorber 1 first absorber 1 through newly-increased solution heat exchanger C and absorption-generator 3 through solution choke valve 13 and absorption-generator 3, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, and first evaporimeter 16 is set up cryogen liquid pump L and is communicated with the newly-increased absorption-evaporimeter J in back with newly-increased absorption-evaporimeter J and has the refrigerant vapour passage to be communicated with first absorber 1 again.
2. on the flow process, refrigerant vapour and heat release that the concentrated solution of branch steam chest 12 enters through second solution pump 7 and increases absorption-evaporimeter J newly, absorbs from first evaporimeter 16 increase the cryogen liquid of absorption-evaporimeter J newly in flowing through, the weak solution of newly-increased absorptions-evaporimeter J enters first absorber 1, absorbs from the refrigerant vapour of newly-increased absorptions-evaporimeter J and heat release in heated medium through newly-increased solution pump E and newly-increased solution heat exchanger C, and the weak solution of first absorber 1 warp increases solution heat exchanger C newly and absorption-generator 3 enters branch steam chest 12; The cryogen liquid that enters first evaporimeter 16 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to newly-increased absorption-evaporimeter J, the second the tunnel after newly-increased cryogen liquid pump K pressurization, flow through again newly-increased absorptions-evaporimeter J, absorb heat into refrigerant vapour and provide to first absorber 1, formation is provided two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to first absorber by absorption-evaporimeter.
Shown in Figure 34, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel the cryogen liquid pipeline that first evaporimeter 16 is communicated with second evaporimeter 17 through second choke valve 20, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased absorber L with dividing steam chest 12 to be communicated with to be adjusted into first generator 4 in first generator 4 through first solution heat exchanger 9 through first solution heat exchanger 9 and absorption-generator 3, newly-increased absorber L also has the weak solution pipeline to be communicated with dividing steam chest 12 through newly-increased solution heat exchanger C and absorption-generator 3, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 to be adjusted into absorption-generator 3 and the weak solution pipeline to be arranged through first solution pump 6, the newly-increased solution heat exchanger C and first solution heat exchanger 9 are communicated with first generator 4, having heated medium pipeline and external communications to be adjusted into first evaporimeter 16 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased cryogen liquid pump K again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the weak solution of absorption-generator 3 enters first generator 4 through first solution pump 6, newly-increased solution heat exchanger C and first solution heat exchanger 9, the concentrated solution of first generator 4 enters newly-increased absorber L, absorbs from the refrigerant vapour of first absorber 1 and heat release in heated medium through first solution heat exchanger 9, and the weak solution of newly-increased absorber L is through newly-increased solution heat exchanger C decrease temperature and pressure, the absorption-generator 3 of flowing through enters branch steam chest 12 again; The cryogen liquid that enters first evaporimeter 16 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to first absorber 1, the second the tunnel after newly-increased cryogen liquid pump K pressurization, flow through again first absorber 1, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 35, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with second generator 5 through first solution heat exchanger 9 in first generator 4 is adjusted into first generator 4 and has the concentrated solution pipeline to be communicated with newly-increased absorber L through first solution heat exchanger 9, newly-increased absorber also has the weak solution pipeline to be communicated with second generator through newly-increased solution pump and newly-increased solution heat exchanger, there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing solution heat exchanger C newly with dividing steam chest 12 to be communicated with to be adjusted into second generator 5 in second generator 5 through second solution heat exchanger 10 and absorption-generator 3, second solution heat exchanger 10 and absorption-generator 3 are communicated with dividing steam chest 12, having heated medium pipeline and external communications to be adjusted into first evaporimeter 16 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased cryogen liquid pump K again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the concentrated solution of first generator 4 enters newly-increased absorber L, absorb from the refrigerant vapour of first absorber 1 and heat release in heated medium, the concentrated solution that the newly-increased solution pump E of weak solution warp of newly-increased absorber L and newly-increased solution heat exchanger C enter second generator, 5, the second generators 5 enters branch steam chest 12 through newly-increased solution heat exchanger C, second solution heat exchanger 10 and absorption-generator 3; One road cryogen liquid of first evaporimeter 16 after newly-increased cryogen liquid pump K pressurization, flow through again first absorber 1, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 36, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel the cryogen liquid pipeline that first evaporimeter 16 is communicated with second evaporimeter 17 through second choke valve 20, increase newly-increased choke valve, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, to absorb-generator 3 has the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 to be adjusted into absorption-generator 3 and to have the weak solution pipeline to be communicated with newly-increased absorber L through first solution pump 6 and newly-increased solution heat exchanger C, newly-increased absorber L also has the weak solution pipeline to be communicated with first generator 4 through the newly-increased solution pump E and first solution heat exchanger 9, there is the concentrated solution pipeline concentrated solution pipeline to be arranged through first solution heat exchanger 9 with dividing steam chest 12 to be communicated with to be adjusted into first generator 4 in first generator 4 through first solution heat exchanger 9 and absorption-generator 3, newly-increased solution heat exchanger C and absorption-generator 3 are communicated with dividing steam chest 12, having heated medium pipeline and external communications to be adjusted into first condenser 14 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased choke valve B again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the weak solution of absorption-generator 3 enters newly-increased absorber L, absorbs from the refrigerant vapour of first absorber 1 and heat release in heated medium through first solution pump 6 and newly-increased solution heat exchanger C, the concentrated solution that the newly-increased solution pump E of weak solution warp of newly-increased absorber L and first solution heat exchanger 9 enter first generator, 4, the first generators 4 enters branch steam chest 12 through first solution heat exchanger 9, newly-increased solution heat exchanger C and absorption-generator 3; The part cryogen liquid of first condenser 14 after newly-increased choke valve B throttling, flow through again first absorber 1, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 37, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel the cryogen liquid pipeline that first evaporimeter 16 is communicated with second evaporimeter 17 through second choke valve 20, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, to divide steam chest 12 to have the concentrated solution pipeline to be communicated with second generator 5 through second solution pump 7 and the 3rd solution heat exchanger 11 is adjusted into branch steam chest 12 and has the concentrated solution pipeline to be communicated with newly-increased absorber L through second solution pump 7 and newly-increased solution heat exchanger C, newly-increased absorber L also has the weak solution pipeline to be communicated with second generator 5 through newly-increased solution pump E and the 3rd solution heat exchanger 11, having the concentrated solution pipeline to be communicated with first absorber 1 through the 3rd solution heat exchanger 11 in second generator 5 is adjusted into second generator 5 and has the concentrated solution pipeline to be communicated with first absorber 1 through the 3rd solution heat exchanger 11 and newly-increased solution heat exchanger C, having heated medium pipeline and external communications to be adjusted into first evaporimeter 16 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased cryogen liquid pump K again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the concentrated solution of dividing steam chest 12 enters newly-increased absorber L, absorbs from the refrigerant vapour of first absorber 1 and heat release in heated medium through second solution pump 7 and newly-increased solution heat exchanger C, the concentrated solution that the newly-increased solution pump E of weak solution warp of newly-increased absorber L and the 3rd solution heat exchanger 11 enter second generator, 5, the second generators 5 enters first absorber 1 through the 3rd solution heat exchanger 11 and newly-increased solution heat exchanger C; The part cryogen liquid of first evaporimeter 16 will increase first absorber 1 of flowing through again after the cryogen liquid pump K pressurization newly, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 38, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 7, the heated medium pipeline of cancellation absorption-generator 3 and external communications, cancel the cryogen liquid pipeline that first evaporimeter 16 is communicated with second evaporimeter 17 through second choke valve 20, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with absorption-generator 3 through second solution heat exchanger 10 second absorber 2 is adjusted into second absorber 2 and has the weak solution pipeline to be communicated with newly-increased absorber L through second solution heat exchanger 10 and newly-increased solution heat exchanger C, newly-increased absorber L also has the weak solution pipeline to be communicated with absorption-generator 3 through newly-increased solution heat exchanger C, having heated medium pipeline and external communications to be adjusted into first evaporimeter 16 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased cryogen liquid pump K again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the weak solution of second absorber 2 enters newly-increased absorber L, absorbs from the refrigerant vapour of first absorber 1 and heat release in heated medium through second solution heat exchanger 10 and newly-increased solution heat exchanger C, and the weak solution of newly-increased absorber L enters absorption-generator 3 through newly-increased solution heat exchanger C; The part cryogen liquid of first evaporimeter 16 will increase first absorber 1 of flowing through again after the cryogen liquid pump K pressurization newly, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 39, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased absorber L with dividing steam chest 12 to be communicated with to be adjusted into second generator 5 in second generator 5 through second solution heat exchanger 10 through second solution heat exchanger 10 and absorption-generator 3, newly-increased absorber L also has the weak solution pipeline to be communicated with dividing steam chest 12 through newly-increased solution heat exchanger C and absorption-generator 3, to absorb-generator 3 has the weak solution pipeline to be communicated with second absorber 2 through the 3rd solution pump 8 and second solution heat exchanger 10 to be adjusted into absorption-generator 3 and the weak solution pipeline to be arranged through the 3rd solution pump 8, the newly-increased solution heat exchanger C and second solution heat exchanger 10 are communicated with second absorber 2, having heated medium pipeline and external communications to be adjusted into first evaporimeter 16 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased cryogen liquid pump K again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the concentrated solution of second generator 5 enters newly-increased absorber L, absorbs from the refrigerant vapour of first absorber 1 and heat release in heated medium through second solution heat exchanger 10, the weak solution of newly-increased absorber L enters branch steam chest 12 through increasing the absorption-generator 3 of flowing through again after solution heat exchanger C step-down is lowered the temperature newly, and the weak solution of absorption-generator 3 enters second absorber 2 through the 3rd solution pump 8, newly-increased solution heat exchanger C and the 3rd solution heat exchanger 10; The part cryogen liquid of first evaporimeter 16 will increase first absorber 1 of flowing through again after the cryogen liquid pump K pressurization newly, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 40, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first absorber to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with first generator 4 through first solution pump 6 and first solution heat exchanger 9 second absorber 2 is adjusted into second absorber 2 and has the weak solution pipeline to be communicated with newly-increased absorber L through newly-increased solution heat exchanger C, newly-increased absorber L also has the weak solution pipeline through first solution pump 6, the newly-increased solution heat exchanger C and first solution heat exchanger 9 are communicated with first generator 4, having heated medium pipeline and external communications to be adjusted into first evaporimeter 16 first absorber 1 sets up the cryogen liquid pipeline and has the refrigerant vapour passage to be communicated with newly-increased absorber L through newly-increased cryogen liquid pump K again with first absorber 1 after first absorber 1 is communicated with, increase absorber L newly and also have heated medium pipeline and external communications.
2. on the flow process, the weak solution of second absorber 2 enters newly-increased absorber L, absorbs from the refrigerant vapour of first absorber 1 and heat release in heated medium through newly-increased solution heat exchanger C, and the weak solution of newly-increased absorber L enters first generator 4 through first solution pump 6, newly-increased solution heat exchanger C and first solution heat exchanger 9; The part cryogen liquid of first evaporimeter 16 will increase first absorber 1 of flowing through again after the cryogen liquid pump K pressurization newly, absorb heat into refrigerant vapour and provide to newly-increased absorber L, form by first absorber and provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing absorber newly.
Shown in Figure 41, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by first generator to newly-increased absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 8, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, first generator 4 had the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into first generator 4 has the refrigerant vapour passage to be communicated with newly-increased absorber L, newly-increased absorber L has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber L through newly-increased solution heat exchanger C, newly-increased generator A also has the refrigerant vapour passage to be communicated with first condenser 14, newly-increased generator A drives thermal medium pipeline and external communications in addition, and newly-increased absorber L also has heated medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first generator 4 produces enters newly-increased absorber L, absorbed also heat release in heated medium by concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber L enters newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, the heating of driving thermal medium enters the solution release refrigerant vapour of newly-increased generator A and provides to first condenser 14, the concentrated solution of newly-increased generator A enters newly-increased absorber L through newly-increased solution heat exchanger C, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first generator.
Shown in Figure 42, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that to first condenser and newly-increased absorber respectively by first generator
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 8, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased choke valve, first generator 4 is set up the refrigerant vapour passage and is communicated with newly-increased absorber L, newly-increased absorber L has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber L through newly-increased solution heat exchanger C, newly-increased generator A also has the refrigerant vapour passage to be communicated with newly-increased condenser M, newly-increased condenser M also has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased choke valve B, newly-increased generator A drives thermal medium pipeline and external communications in addition, and newly-increased absorber L and newly-increased condenser M also have heated medium pipeline and external communications respectively.
2. on the flow process, the part refrigerant vapour that first generator 4 produces enters newly-increased absorber L, absorbed also heat release in heated medium by concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber L enters newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, the heating of driving thermal medium enters the solution release refrigerant vapour of newly-increased generator A and provides to newly-increased condenser M, the refrigerant vapour heat release that enters newly-increased condenser M becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser M enters first condenser 14 through newly-increased choke valve B throttling, the concentrated solution of newly-increased generator A enters newly-increased absorber L through newly-increased solution heat exchanger C, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first condenser and newly-increased absorber respectively by first generator.
Shown in Figure 43, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that by newly-increased generator to first absorber
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 8, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorber L, newly-increased absorber L has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber L through newly-increased solution heat exchanger C, newly-increased generator A also has the refrigerant vapour passage to be communicated with first absorber 1, newly-increased generator A drives thermal medium pipeline and external communications in addition, and newly-increased absorber L also has heated medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that first evaporimeter 16 produces enters newly-increased absorber L, absorbed also heat release in heated medium by concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber L enters newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, the heating of driving thermal medium enters the solution release refrigerant vapour of newly-increased generator A and provides to first absorber 1, the concentrated solution of newly-increased generator A enters newly-increased absorber L through newly-increased solution heat exchanger C, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased generator.
Shown in Figure 44, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that to the newly-increased condenser and first absorber respectively by newly-increased generator
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 43, increase newly-increased condenser and newly-increased choke valve, newly-increased generator A sets up the refrigerant vapour passage and is communicated with newly-increased condenser M, increasing condenser M newly also has the cryogen liquid pipeline through newly-increased choke valve B and first evaporimeter, 16 connected sums heated medium pipeline and external communications to be arranged respectively, forms by newly-increased generator and provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing the condenser and first absorber newly respectively.
Shown in Figure 45, provide two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to be achieved in that to first absorber jointly by newly-increased absorption-evaporimeter and newly-increased generator
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 8, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased absorption-evaporimeter, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter 16 had the refrigerant vapour passage to be communicated with first absorber 1 to be adjusted into first evaporimeter 16 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter J, newly-increased absorption-evaporimeter J also has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter J through newly-increased solution heat exchanger C, first evaporimeter 16 is set up cryogen liquid pipeline newly-increased absorption-evaporimeter J after increasing cryogen liquid pump K newly and newly-increased absorption-evaporimeter J is communicated with has the refrigerant vapour passage to be communicated with first absorber 1 again, and newly-increased generator A also has refrigerant vapour passage and first absorber, 1 connected sum that the thermal medium pipeline of driving and external communications are arranged respectively.
2. on the flow process, the refrigerant vapour that first evaporimeter 16 produces enters and increase absorber L newly, absorbed by the concentrated solution from newly-increased generator A and heat release increases the cryogen liquid of absorption-evaporimeter J newly in flowing through, the weak solution of newly-increased absorber L enters newly-increased generator A through newly-increased solution pump E and newly-increased solution heat exchanger C, the heating of driving thermal medium enters the solution release refrigerant vapour of newly-increased generator A and provides to first absorber 1, and the newly-increased solution heat exchanger C of concentrated solution warp of newly-increased generator A enters newly-increased absorber L; One road cryogen liquid of first evaporimeter 16 after newly-increased cryogen liquid pump K pressurization, flow through again newly-increased absorptions-evaporimeter J, absorb heat into refrigerant vapour and provide to first absorber 1, form by newly-increased generator and increase absorption-evaporimeter provides refrigerant vapour jointly to first absorber two-stage multiterminal heat supply the 3rd class absorption heat pump newly.
Shown in Figure 46, be that two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order is achieved in that with economic benefits and social benefits
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 14, increase newly-increased second generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase generator A newly has the refrigerant vapour passage to be communicated with first condenser 14 to be adjusted into newly-increased generator A to have the refrigerant vapour passage to be communicated with newly-increased absorber L, newly-increased absorber L has the weak solution pipeline to be communicated with the newly-increased second generator F through newly-increased solution pump E and newly-increased solution heat exchanger C, the newly-increased second generator F also has the concentrated solution pipeline to be communicated with newly-increased absorber L through newly-increased solution heat exchanger C, the newly-increased second generator F also has refrigerant vapour passage and first condenser, 14 connected sums that the thermal medium pipeline of driving and external communications are arranged respectively, and newly-increased absorber L also has heated medium pipeline and external communications.
2. on the flow process, the refrigerant vapour that the newly-increased first generator A produces enters newly-increased absorber L, absorbed also heat release in heated medium by concentrated solution from the newly-increased second generator F, the weak solution of newly-increased absorber L enters the newly-increased second generator F through newly-increased solution pump E and newly-increased solution heat exchanger C, the heating of driving thermal medium enters the solution release refrigerant vapour of the newly-increased second generator F and provides to first condenser 14, the concentrated solution of the newly-increased second generator F enters newly-increased absorber L through newly-increased solution heat exchanger C, and forming with the single-stage economic benefits and social benefits is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
Shown in Figure 47, be that two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order is achieved in that with economic benefits and social benefits
1. on the structure, in multiterminal heat supply the 3rd class absorption heat pump shown in Figure 14, increase newly-increased second generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the 3rd choke valve, newly-increased generator A sets up the refrigerant vapour passage and is communicated with newly-increased absorber L, newly-increased absorber L has the weak solution pipeline to be communicated with the newly-increased second generator F through newly-increased solution pump E and newly-increased solution heat exchanger C, the newly-increased second generator F also has the concentrated solution pipeline to be communicated with newly-increased absorber L through newly-increased solution heat exchanger C, the newly-increased second generator F also has refrigerant vapour passage and newly-increased condenser M connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased condenser M also has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased the 3rd choke valve G, and newly-increased absorber L and newly-increased condenser M also have heated medium pipeline and external communications respectively.
2. on the flow process, the part refrigerant vapour that the newly-increased first generator A produces enters newly-increased absorber L, absorbed also heat release in heated medium by concentrated solution from the newly-increased second generator F, the weak solution of newly-increased absorber L enters the newly-increased second generator F through newly-increased solution pump E and newly-increased solution heat exchanger C, the heating of driving thermal medium enters the solution release refrigerant vapour of the newly-increased second generator F and provides to newly-increased condenser M, the refrigerant vapour heat release that enters newly-increased condenser M becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser M enters first condenser 14 through newly-increased the 3rd choke valve G throttling, the concentrated solution of the newly-increased second generator F enters newly-increased absorber L through newly-increased solution heat exchanger C, and forming with the single-stage economic benefits and social benefits is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
Single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump shown in Figure 48, that be additional high-temperature heat supply end with newly-increased condenser is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 14, increase newly-increased condenser and newly-increased the 4th choke valve, first generator 4 is set up the refrigerant vapour passage and is communicated with newly-increased condenser M, newly-increased condenser M also has the cryogen liquid pipeline to be communicated with first condenser 14 through newly-increased the 4th choke valve P, and newly-increased condenser M also has heated medium pipeline and external communications; The part refrigerant vapour that first generator 4 produces enters newly-increased condenser M, heat release becomes cryogen liquid in heated medium, the cryogen liquid of newly-increased condenser M enters first condenser 14 through newly-increased the 4th choke valve P throttling, forms with multiterminal heat supply three class absorption heat pump of newly-increased condenser for additional high-temperature heat supply end.
Adjustable type single-stage single-action multiterminal heat supply the 3rd class absorption heat pump shown in Figure 49 is achieved in that
In multiterminal heat supply the 3rd class absorption heat pump shown in Figure 9, increase the first flow control valve and second flow control valve, with first condenser 14 have heated medium pipeline and external communications be adjusted into the outside have the heated medium pipeline be communicated with first condenser 14 back first condenser 14 have the heated medium pipeline to be communicated with second absorber 2 with external communications with through the second flow control valve O through first flow choke valve N respectively again, having heated medium pipeline and external communications to be adjusted into first condenser 14 second absorber 2 has heated medium pipeline second absorber 2 after the second flow choke valve O and second absorber 2 and external communications that heated medium pipeline and external communications are arranged again, forms adjustable type multiterminal heat supply the 3rd class absorption heat pump.
The effect that the technology of the present invention can realize---backheating type absorption-generation systems and multiterminal heat supply the 3rd class absorption heat pump proposed by the invention have following effect and advantage:
1. backheating type absorption-the generation systems that proposes, rational in infrastructure, the backheat amplitude can be regulated.
2. serial multiterminal heat supply the 3rd class absorption heat pump that proposes can utilize the residual heat resources of lower temperature, improves the residual heat resources utilization rate.
3. serial multiterminal heat supply the 3rd class absorption heat pump that proposes has enriched absorption heat pump, can realize better that heat pump heat supply and user use the mutual coupling between heat.
4. utilize serial multiterminal heat supply the 3rd class absorption heat pump provided by the invention, can make the continuous correspondence between single unit running parameter and the performance index, can realize that the nothing on running parameter and performance index is interrupted linking between the adjacent unit.
5. serial multiterminal heat supply the 3rd class absorption heat pump that proposes can be selected according to the height of waste heat parameter and heat supply temperature the degree of backheat, is conducive to keep the superior performance index, improves efficiency of energy utilization.

Claims (81)

1. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, the 3rd solution heat exchanger and branch steam chest are formed, first absorber (1) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10), second absorber (2) also has the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10), absorption-generator (3) also has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9), first generator (4) also has the concentrated solution pipeline to be communicated with dividing steam chest (12) through first solution heat exchanger (9) and absorption-generator (3), divide steam chest (12) to also have the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11), second generator (5) also has the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11), first absorber (1) also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber (2) also has heated medium pipeline and external communications, second generator (5) also has refrigerant vapour passage and second absorber (2) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest (12) to also have refrigerant vapour passage and external communications, absorption-generator (3) also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator (4) also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms single channel solution and loops back hot type absorption-generation systems; Wherein, when not having second generator and the 3rd solution heat exchanger, second generator (5) has the refrigerant vapour passage to be communicated with second absorber (2) to change to first generator (4) to increase the refrigerant vapour passage to be communicated with second absorber (2), and branch steam chest (12) has the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11), second generator (5) has the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) to change to branch steam chest (12) and have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) again.
2. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, the 3rd solution heat exchanger and branch steam chest are formed, first absorber (1) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10), second absorber (2) also has the weak solution pipeline to be communicated with dividing steam chest (12) through second solution heat exchanger (10) and absorption-generator (3), divide steam chest (12) to also have the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11), second generator (5) also has the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11), absorption-generator (3) also has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9), first generator (4) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9), first absorber (1) also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber (2) also has heated medium pipeline and external communications, second generator (5) also has refrigerant vapour passage and second absorber (2) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest (12) to also have refrigerant vapour passage and external communications, absorption-generator (3) also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator (4) also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms two-way solution and loops back hot type absorption-generation systems; Wherein, when not having second generator and the 3rd solution heat exchanger, second generator (5) has the refrigerant vapour passage to be communicated with second absorber (2) to change to first generator (4) to increase the refrigerant vapour passage to be communicated with second absorber (2), and branch steam chest (12) has the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11), second generator (5) has the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) to change to branch steam chest (12) and have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) again.
3. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger and branch steam chest are formed, first absorber (1) has the weak solution pipeline to be communicated with absorption-generator (3), absorption-generator (3) also has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10), second absorber (2) also has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9), first generator (4) also has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9), second generator (5) also has the concentrated solution pipeline to be communicated with dividing steam chest (12) through second solution heat exchanger (10) and absorption-generator (3), divide steam chest (12) to also have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7), first absorber (1) also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber (2) also has heated medium pipeline and external communications, second generator (5) also has refrigerant vapour passage and second absorber (2) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest (12) to also have refrigerant vapour passage and external communications, absorption-generator (3) also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator (4) also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms single channel solution and loops back hot type absorption-generation systems; Wherein, when not having second generator, second generator (5) has the refrigerant vapour passage to be communicated with second absorber (2) to change to first generator (4) to increase the refrigerant vapour passage to be communicated with second absorber (2), and first generator (4) has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9), second generator (5) has the concentrated solution pipeline concentrated solution pipeline to be arranged through first solution heat exchanger (9) through second solution heat exchanger (10) and absorption-generator (3) with dividing steam chest (12) to be communicated with to change to first generator (4) again, second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12).
4. back-heating type absorption-generation systems, mainly by first absorber, second absorber, absorption-generator, first generator, second generator, first solution pump, second solution pump, the 3rd solution pump, first solution heat exchanger, second solution heat exchanger, divide steam chest and solution choke valve to form, first absorber (1) has the weak solution pipeline to be communicated with dividing steam chest (12) through solution choke valve (13) and absorption-generator (3), divide steam chest (12) to also have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7), absorption-generator (3) also has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10), second absorber (2) also has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9), first generator (4) also has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9), second generator (5) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10), first absorber (1) also has refrigerant vapour passage and external communications respectively and heated medium pipeline and external communications is arranged, second absorber (2) also has heated medium pipeline and external communications, second generator (5) also has refrigerant vapour passage and second absorber (2) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, divide steam chest (12) to also have refrigerant vapour passage and external communications, absorption-generator (3) also has refrigerant vapour passage and external communications or refrigerant vapour passage and external communications is also arranged respectively and heated medium pipeline and external communications are arranged, first generator (4) also has refrigerant vapour passage and external communications respectively and the thermal medium pipeline of driving and external communications is arranged, and forms two-way solution and loops back hot type absorption-generation systems; Wherein, when not having second generator, second generator (5) has the refrigerant vapour passage to be communicated with second absorber (2) to change to first generator (4) to increase the refrigerant vapour passage to be communicated with second absorber (2), and first generator (4) has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9), second generator (5) has the concentrated solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10) to change to first generator (4) and have the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) again.
5. multiterminal heat supply the 3rd class absorption heat pump, be described in claim 1, in the back-heating type absorption-generation systems of no heated medium pipeline of absorption-generator (3) and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through choke valve (18), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through cryogen liquid pump (19), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein: 1. can select have the cryogen liquid pipeline to be communicated with second evaporimeter (17) second condenser (15) and be adjusted into second condenser (15) and have the cryogen liquid pipeline to be communicated with first evaporimeter (16), increase by second choke valve (20) again and set up the cryogen liquid pipeline and be communicated with second evaporimeter (17) through second choke valve (20) by first evaporimeter (16) through cryogen liquid pump (19) through cryogen liquid pump (19); When 2. not having second evaporimeter (17), have the cryogen liquid pipeline to be communicated with second evaporimeter (17) through cryogen liquid pump (19) second condenser (15) and be adjusted into second condenser (15) and have the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3).
6. multiterminal heat supply the 3rd class absorption heat pump, be described in claim 1, absorption-generator (3) has in the back-heating type absorption-generation systems of heated medium pipeline and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through first throttle valve (18), first evaporimeter (16) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through second choke valve (20), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) or first evaporimeter (16) through cryogen liquid pump (19), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter (17), having the cryogen liquid pipeline to be communicated with second evaporimeter (17) or first evaporimeter (16) through cryogen liquid pump (19) second condenser (15) is defined as second condenser (15) and has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), cancel the cryogen liquid pipeline that first evaporimeter (16) is communicated with second evaporimeter (17) through second choke valve (20), first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3).
7. multiterminal heat supply the 3rd class absorption heat pump, be in the described back-heating type absorption-generation systems of claim 2, when 1. second generator and the 3rd solution heat exchanger are arranged, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through choke valve (18), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter (17), have the cryogen liquid pipeline to be communicated with second evaporimeter (17) through choke valve (18) first condenser (14) and be adjusted into first condenser (14) and have the cryogen liquid pipeline to be communicated with first evaporimeter (16) through choke valve (18), first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3); When 2. not having second generator and the 3rd solution heat exchanger, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through first throttle valve (18), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), first evaporimeter (16) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through second choke valve (20), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter and second choke valve, cancel the cryogen liquid pipeline that first evaporimeter (16) is communicated with second evaporimeter (17) through second choke valve (20), first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3).
8. multiterminal heat supply the 3rd class absorption heat pump, be described in claim 3, in the back-heating type absorption-generation systems of no heated medium pipeline of absorption-generator (3) and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve, cryogen liquid pump and solution choke valve, first absorber (1) had the weak solution pipeline to be communicated with absorption-generator (3) to be adjusted into first absorber (1) has the weak solution pipeline to be communicated with absorption-generator (3) through solution choke valve (13), having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through choke valve (18), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through cryogen liquid pump (19), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein: 1. can select have the cryogen liquid pipeline to be communicated with second evaporimeter (17) second condenser (15) and be adjusted into second condenser (15) and have the cryogen liquid pipeline to be communicated with first evaporimeter (16), increase by second choke valve (20) again and set up the cryogen liquid pipeline and be communicated with second evaporimeter (17) through second choke valve (16) by first evaporimeter (16) through cryogen liquid pump (19) through cryogen liquid pump (19); When 2. not having second evaporimeter (17) and solution choke valve (13), having the cryogen liquid pipeline to be communicated with second evaporimeter (17) through cryogen liquid pump (19) second condenser (15) is adjusted into second condenser (15) and has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), first absorber (1) has the weak solution pipeline to be communicated with absorption-generator (3), and first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3).
9. multiterminal heat supply the 3rd class absorption heat pump, be described in claim 3, absorption-generator (3) has in the back-heating type absorption-generation systems of heated medium pipeline and external communications, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, the first throttle valve, second choke valve, cryogen liquid pump and solution choke valve, first absorber (1) had the weak solution pipeline to be communicated with absorption-generator (3) to be adjusted into first absorber (1) has the weak solution pipeline to be communicated with absorption-generator (3) through solution choke valve (13), having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through first throttle valve (18), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) or second evaporimeter (17) through cryogen liquid pump (19), first evaporimeter (16) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through second choke valve (20), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter (17) and solution choke valve (13), having the cryogen liquid pipeline to be communicated with first evaporimeter (16) or second evaporimeter (17) through cryogen liquid pump (19) second condenser (15) is defined as second condenser (15) and has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), cancel the cryogen liquid pipeline that first evaporimeter (16) is communicated with second evaporimeter (17) through second choke valve (20), first absorber (1) has the weak solution pipeline to be communicated with absorption-generator (3), and first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3).
10. multiterminal heat supply the 3rd class absorption heat pump, be in the described back-heating type absorption-generation systems of claim 4, increase by first condenser, second condenser, first evaporimeter, second evaporimeter, choke valve and cryogen liquid pump, having refrigerant vapour passage and external communications to be defined as first generator (4) in first generator (4) has the refrigerant vapour passage to be communicated with first condenser (14), first condenser (14) also has the cryogen liquid pipeline to be communicated with second evaporimeter (17) through choke valve (18), to absorb-generator (3) has refrigerant vapour passage and external communications to be defined as second evaporimeter (17) to have the refrigerant vapour passage to be communicated with absorption-generator (3), to divide steam chest (12) to have refrigerant vapour passage and external communications to be defined as branch steam chest (12) has the refrigerant vapour passage to be communicated with second condenser (15), second condenser (15) also has the cryogen liquid pipeline to be communicated with first evaporimeter (16) through cryogen liquid pump (19), having refrigerant vapour passage and external communications to be defined as first evaporimeter (16) first absorber (1) has the refrigerant vapour passage to be communicated with first absorber (1), first condenser (14) also has heated medium pipeline and external communications, second condenser (15) also has cooling medium pipeline and external communications, first evaporimeter (16) and second evaporimeter (17) also have surplus heat respectively medium pipeline and external communications form single-stage single-action multiterminal heat supply the 3rd class absorption heat pump; Wherein, when not having second evaporimeter (17), have the cryogen liquid pipeline to be communicated with second evaporimeter (17) through choke valve (18) first condenser (14) and be adjusted into first condenser (14) and have the cryogen liquid pipeline to be communicated with first evaporimeter (16) through choke valve (18), first evaporimeter (16) increases the refrigerant vapour passage and is communicated with absorption-generator (3).
11. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to converge through first solution heat exchanger (9) concentrated solution pipeline afterwards with first generator (4) through newly-increased solution heat exchanger (C), be communicated with dividing steam chest (12) through absorption-generator (3) again, having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
12. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
13. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-10, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to converge through first solution heat exchanger (9) concentrated solution pipeline afterwards with first generator (4) afterwards through newly-increased solution heat exchanger (C), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage parallel double-effect multiterminal heat supply the 3rd class absorption heat pump.
14. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased generator (A) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4) in first generator (4) through increasing solution heat exchanger (C) newly through first solution heat exchanger (9) and absorption-generator (3), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with dividing steam chest (12) through first solution heat exchanger (9) and absorption-generator (3), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through first solution pump (6), first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
15. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through first solution pump (6), first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
16. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with first generator (4), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with first generator (4), first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with newly-increased generator (A) through increasing solution heat exchanger (C) newly with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), newly-increased generator (A) also has the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
17. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with first generator (4), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with first generator (4), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
18. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6) and first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing solution heat exchanger (C) newly with dividing steam chest (12) to be communicated with to be adjusted into first generator (4) in first generator (4) through first solution heat exchanger (9) and absorption-generator (3), first solution heat exchanger (9) and absorption-generator (3) are communicated with dividing steam chest (12), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
19. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6) and first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C) and first solution heat exchanger (9), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump.
20. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6) and first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased solution heat exchanger (C) and first solution heat exchanger (9), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased solution heat exchanger (C); When 2. not having second generator, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6) and first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline through increasing solution heat exchanger (C) newly with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with dividing steam chest (12) through newly-increased solution heat exchanger (C), second solution heat exchanger (10) and absorption-generator (3).
21. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6) and first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased solution heat exchanger (C) and first solution heat exchanger (9), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased solution heat exchanger (C); When 2. not having second generator, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6) and first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger (C), first solution heat exchanger (9) and second solution heat exchanger (10) are communicated with absorption-generator (3), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have the refrigerant vapour passage to be communicated with the newly-increased generator (A) in back with newly-increased generator (A) in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage series connection economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased generator (A) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C) and second solution heat exchanger (10).
22. multiterminal heat supply the 3rd class absorption heat pump, be in described at claim 11-21, that second generator is arranged multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased second choke valve (D), second generator (5) had drive thermal medium pipeline and external communications and be adjusted into first generator (4) and set up the refrigerant vapour passage and is communicated with back second generator (5) with second generator (5) and has cryogen liquid pipeline warp to increase second choke valve (D) newly again to be communicated with formation single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump with first condenser (14).
23. multiterminal heat supply the 3rd class absorption heat pump, be in described at claim 11-21, as not have second generator multiterminal heat supply the 3rd class absorption heat pump, there is the refrigerant vapour passage to be communicated with to be adjusted into newly-increased first generator (A) to set up the refrigerant vapour passage in first generator (4) and is communicated with, formation single-stage economic benefits and social benefits multiterminal heat supply the 3rd class absorption heat pump with second absorber (2) with second absorber (2).
24. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased second generator (F) through newly-increased second solution heat exchanger (H) with newly-increased first generator (A) connected sum through newly-increased first solution heat exchanger (C) respectively, newly-increased first generator (A) has the concentrated solution pipeline to have the concentrated solution pipeline all to converge through first solution heat exchanger (9) concentrated solution pipeline afterwards with first generator (4) afterwards through newly-increased second solution heat exchanger (H) with newly-increased second generator (F) afterwards through newly-increased first solution heat exchanger (C), be communicated with dividing steam chest (12) through absorption-generator (3) again, having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator (A) newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
25. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased second generator (F) through newly-increased second solution heat exchanger (H) with newly-increased first generator (A) connected sum through newly-increased first solution heat exchanger (C) respectively, newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased second solution heat exchanger (H), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
26. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-10, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased second generator (F) through newly-increased second solution heat exchanger (H) with newly-increased first generator (A) connected sum through newly-increased first solution heat exchanger (C) respectively, newly-increased first generator (A) also has the concentrated solution pipeline to converge through first solution heat exchanger (9) concentrated solution pipeline afterwards with first generator (4) afterwards through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to converge through first solution heat exchanger (9) concentrated solution pipeline afterwards with first generator (4) afterwards through newly-increased second solution heat exchanger (H), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage triple effect multiterminal in parallel heat supply the 3rd class absorption heat pump.
27. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased first generator (A) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4) in first generator (4) through first solution heat exchanger (9) through first solution heat exchanger (9) and absorption-generator (3), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with newly-increased second generator (F) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with dividing steam chest (12) through newly-increased second solution heat exchanger (H) and absorption-generator (3), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through first solution pump (6), newly-increased second solution heat exchanger (H), newly-increased first solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
28. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through first solution heat exchanger (9), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with newly-increased second generator (F) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased second solution heat exchanger (H), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through first solution pump (6), newly-increased second solution heat exchanger (H), newly-increased first solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
29. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through first solution heat exchanger (9), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with newly-increased second generator (F) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased second solution heat exchanger (H), having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), newly-increased second solution heat exchanger (H), newly-increased first solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with newly-increased first generator (A) through first solution heat exchanger (9) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with newly-increased second generator (F) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline through newly-increased second solution heat exchanger (H), second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12), having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), newly-increased second solution heat exchanger (H), newly-increased first solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
30. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through first solution heat exchanger (9), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with newly-increased second generator (F) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased second solution heat exchanger (H), having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), newly-increased second solution heat exchanger (H), newly-increased first solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator (A) newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger and newly-increased second solution heat exchanger, having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through first solution heat exchanger (9), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with newly-increased second generator (F) through newly-increased first solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased second solution heat exchanger (H) and second solution heat exchanger (10), having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and the weak solution pipeline is arranged through first solution pump (6), newly-increased second solution heat exchanger (H), newly-increased first solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
31. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6) and first solution heat exchanger (9), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (I) and newly-increased second solution heat exchanger (H), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased first solution pump (E) and newly-increased first solution heat exchanger (C), there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing first solution heat exchanger (C) newly with dividing steam chest (12) to be communicated with to be adjusted into first generator (4) in first generator (4) through first solution heat exchanger (9) and absorption-generator (3), newly-increased second solution heat exchanger (H), first solution heat exchanger (9) and absorption-generator (3) are communicated with dividing steam chest (12), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
32. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6) and first solution heat exchanger (9), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (I) and newly-increased second solution heat exchanger (H), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased first solution pump (E) and newly-increased first solution heat exchanger (C), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger (C), newly-increased second solution heat exchanger (H) and first solution heat exchanger (9) are communicated with absorption-generator (3), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator (A) newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump.
33. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6) and first solution heat exchanger (9), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (I) and newly-increased second solution heat exchanger (H), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased first solution pump (E) and newly-increased first solution heat exchanger (C), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger (C), newly-increased second solution heat exchanger (H) and first solution heat exchanger (9) are communicated with second generator (5), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased first solution heat exchanger (C) and newly-increased second solution heat exchanger (H); When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6) and first solution heat exchanger (9), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (I) and newly-increased second solution heat exchanger (H), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased first solution pump (E) and newly-increased first solution heat exchanger (C), first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline through increasing first solution heat exchanger (C) newly with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), newly-increased second solution heat exchanger (H), first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator (A) newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with dividing steam chest (12) through newly-increased first solution heat exchanger (C), newly-increased second solution heat exchanger (H), second solution heat exchanger (10) and absorption-generator (3).
34. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6) and first solution heat exchanger (9), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (I) and newly-increased second solution heat exchanger (H), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased first solution pump (E) and newly-increased first solution heat exchanger (C), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger (C), newly-increased second solution heat exchanger (H) and first solution heat exchanger (9) are communicated with second generator (5), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator (A) newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with second generator (5) through newly-increased first solution heat exchanger (C) and newly-increased second solution heat exchanger (H); When 2. not having second generator, increase newly-increased first generator, newly-increased second generator, newly-increased first throttle valve, newly-increased second choke valve, newly-increased first solution heat exchanger, newly-increased second solution heat exchanger, newly-increased first solution pump and newly-increased second solution pump, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6) and first solution heat exchanger (9), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased first generator (A) through newly-increased second solution pump (I) and newly-increased second solution heat exchanger (H), newly-increased first generator (A) also has the concentrated solution pipeline to be communicated with first generator (4) through newly-increased first solution pump (E) and newly-increased first solution heat exchanger (C), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and the concentrated solution pipeline is arranged through newly-increased first solution heat exchanger (C), newly-increased second solution heat exchanger (H), first solution heat exchanger (9) and second solution heat exchanger (10) are communicated with absorption-generator (3), having the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) to have refrigerant vapour passage and newly-increased first generator (A) to be communicated with newly-increased first generator (A) in back in first generator (4) has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased first throttle valve (B) again---and the refrigerant vapour of first generator generation is as the driving thermal medium that increases first generator (A) newly, increasing second generator (F) newly after newly-increased first generator (A) also has refrigerant vapour passage and newly-increased second generator (F) to be communicated with has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased second choke valve (D) again---the driving thermal medium of newly-increased second generator of refrigerant vapour conduct of newly-increased first generator generation, newly-increased second generator (F) also has the refrigerant vapour passage to be communicated with first condenser (14), forms single-stage serially connected three-effect multiterminal heat supply the 3rd class absorption heat pump; Wherein, when selecting cancellation first solution heat exchanger (9), second absorber (2) has the weak solution pipeline to be communicated with newly-increased second generator (F) through first solution pump (6), and first generator (4) has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased first solution heat exchanger (C), newly-increased second solution heat exchanger (H) and second solution heat exchanger (10).
35. multiterminal heat supply the 3rd class absorption heat pump, be in described at claim 24-34, that second generator is arranged multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve (G), second generator (5) had drive thermal medium pipeline and external communications and be adjusted into first generator (4) and set up the refrigerant vapour passage and is communicated with back second generator (5) with second generator (5) and has cryogen liquid pipeline warp to increase the 3rd choke valve (G) newly again to be communicated with formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with first condenser (14).
36. multiterminal heat supply the 3rd class absorption heat pump, be in described at claim 24-34, that second generator is arranged multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve (G), second generator (5) had drive thermal medium pipeline and external communications and be adjusted into newly-increased first generator (A) and set up the refrigerant vapour passage and is communicated with back second generator (5) with second generator (5) and has cryogen liquid pipeline warp to increase the 3rd choke valve (G) newly again to be communicated with formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with first condenser (14).
37. multiterminal heat supply the 3rd class absorption heat pump, be in described at claim 24-34, as not have second generator multiterminal heat supply the 3rd class absorption heat pump, there is the refrigerant vapour passage to be communicated with to be adjusted into newly-increased first generator (A) to set up the refrigerant vapour passage in generator (4) and is communicated with, formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with second absorber (2) with second absorber (2).
38. multiterminal heat supply the 3rd class absorption heat pump, be in described at claim 24-34, as not have second generator multiterminal heat supply the 3rd class absorption heat pump, there is the refrigerant vapour passage to be communicated with to be adjusted into newly-increased second generator (F) to set up the refrigerant vapour passage in generator (4) and is communicated with, formation single-stage triple effect multiterminal heat supply the 3rd class absorption heat pump with second absorber (2) with second absorber (2).
39. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through newly-increased solution heat exchanger (C), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) again, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11) is adjusted into branch steam chest (12) and the concentrated solution pipeline is arranged through second solution pump (7), newly-increased second solution heat exchanger (C) and the 3rd solution heat exchanger (11) are communicated with second generator 5, first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorptions-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through newly-increased solution heat exchanger (C), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) again, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) and newly-increased solution heat exchanger (C), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorptions-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
40. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) in second generator (5) is adjusted into second generator (5) and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through the 3rd solution heat exchanger (11), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C) again, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and the weak solution pipeline is arranged through newly-increased solution heat exchanger (C), the 3rd solution pump (8) and second solution heat exchanger (10) are communicated with second absorber (2), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorptions-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through second solution pump (7), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C) again, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and the weak solution pipeline is arranged through newly-increased solution heat exchanger (C), the 3rd solution pump (8) and second solution heat exchanger (10) are communicated with second absorber (2), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorptions-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
41. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through newly-increased solution heat exchanger (C), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) again, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11) is adjusted into branch steam chest (12) and the concentrated solution pipeline is arranged through second solution pump (7), newly-increased second solution heat exchanger (C) and the 3rd solution heat exchanger (11) are communicated with second generator 5, first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through newly-increased solution heat exchanger (C), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) again, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) and newly-increased solution heat exchanger (C), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
42. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) in second generator (5) is adjusted into second generator (5) and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through the 3rd solution heat exchanger (11), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C) again, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and the weak solution pipeline is arranged through newly-increased solution heat exchanger (C), the 3rd solution pump (8) and second solution heat exchanger (10) are communicated with second absorber (2), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through second solution pump (7), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C) again, having the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) first absorber (1) is adjusted into first absorber (1) and the weak solution pipeline is arranged through newly-increased solution heat exchanger (C), the 3rd solution pump (8) and second solution heat exchanger (10) are communicated with second absorber (2), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
43. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with absorptions-generator (3) directly or through solution choke valve (13) first absorber (1) is adjusted into first absorber (1) and has weak solution pipeline warp to increase solution heat exchanger (C) newly to be communicated with newly-increased absorption-evaporimeter (J), newly-increased absorption-evaporimeter (J) has the weak solution pipeline directly or through solution choke valve (13) to be communicated with absorption-generator (3) again, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) and newly-increased solution heat exchanger (C), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorptions-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
44. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, cancellation solution choke valve, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, having the weak solution pipeline to be communicated with absorptions-generator (3) directly or through solution choke valve (13) first absorber (1) is adjusted into first absorber (1) and has weak solution pipeline warp to increase solution heat exchanger (C) newly to be communicated with absorption-generator (3), to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through second solution pump (7), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C) again, first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorptions-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), formation provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to first absorber.
45. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter and newly-increased solution heat exchanger, there is the weak solution pipeline to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) with dividing steam chest (12) to be communicated with to be adjusted into first absorber (1) first absorber (1) through increasing solution heat exchanger (C) newly through solution choke valve (13) and absorption-generator (3), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with dividing steam chest (12) through solution choke valve (13) and absorption-generator (3) again, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) and newly-increased solution heat exchanger (C), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
46. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, increase newly-increased cryogen liquid pump, newly-increased absorption-evaporimeter, newly-increased solution heat exchanger and newly-increased solution pump, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through second solution pump (7), newly-increased absorption-evaporimeter (J) has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C) again, cancellation solution choke valve (13), there is the weak solution pipeline to have the weak solution pipeline to be communicated with branch steam chest (12) with dividing steam chest (12) to be communicated with to be adjusted into first absorber (1) first absorber (1) through newly-increased solution heat exchanger (C) and absorption-generator (3) through solution choke valve (13) and absorption-generator (3), first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased absorption-evaporimeter.
47. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased absorber (L) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4) in first generator (4) through first solution heat exchanger (9) through first solution heat exchanger (9) and absorption-generator (3), newly-increased absorber (L) also has the weak solution pipeline to be communicated with dividing steam chest (12) through newly-increased solution heat exchanger (C) and absorption-generator (3), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through first solution pump (6), newly-increased solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
48. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9), newly-increased absorber (L) also has the weak solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C), to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through first solution pump (6), newly-increased solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L).
49. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9), newly-increased absorber (L) also has the weak solution pipeline to be communicated with second generator (5) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), there is the concentrated solution pipeline concentrated solution pipeline to be arranged through increasing solution heat exchanger (C) newly with dividing steam chest (12) to be communicated with to be adjusted into second generator (5) in second generator (5) through second solution heat exchanger (10) and absorption-generator (3), second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased absorber, first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), newly-increased absorber (L) also has the weak solution pipeline to be communicated with dividing steam chest (12) through second solution heat exchanger (10) and absorption-generator (3), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
50. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9), newly-increased absorber (L) also has the weak solution pipeline to be communicated with second generator (5) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10) in second generator (5) is adjusted into second generator (5) and has the concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C) and second solution heat exchanger (10), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L); When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9), newly-increased absorber (L) also has the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L).
51. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with newly-increased absorber (L) through first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and first solution heat exchanger (9), there is the concentrated solution pipeline concentrated solution pipeline to be arranged through first solution heat exchanger (9) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4) in first generator (4) through first solution heat exchanger (9) and absorption-generator (3), newly-increased solution heat exchanger (C) and absorption-generator (3) are communicated with dividing steam chest (12), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
52. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, to absorb-generator (3) has the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) to be adjusted into absorption-generator (3) and to have the weak solution pipeline to be communicated with newly-increased absorber (L) through first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and first solution heat exchanger (9), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L).
53. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and first solution heat exchanger (9), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) and newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and first solution heat exchanger (9), first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline through first solution heat exchanger (9) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), newly-increased solution heat exchanger (C), second solution heat exchanger (10) and absorption-generator (3) are communicated with dividing steam chest (12), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
54. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and first solution heat exchanger (9), having the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with second generator (5) through first solution heat exchanger (9) and newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L); When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first generator (4) through newly-increased solution pump (E) and first solution heat exchanger (9), having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and the concentrated solution pipeline is arranged through first solution heat exchanger (9), newly-increased solution heat exchanger (C) and second solution heat exchanger (10) are communicated with absorption-generator (3), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L).
55. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through second solution pump (7) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with second generator (5) through newly-increased solution pump (E) and the 3rd solution heat exchanger (11), having the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) in second generator (5) is adjusted into second generator (5) and has the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) and newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through second solution pump (7) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
56. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, when 1. second generator and the 3rd solution heat exchanger are arranged, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with second generator (5) through second solution pump (7) and the 3rd solution heat exchanger (11) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through second solution pump (7) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with second generator (5) through newly-increased solution pump (E) and the 3rd solution heat exchanger (11), having the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) in second generator (5) is adjusted into second generator (5) and has the concentrated solution pipeline to be communicated with first absorber (1) through the 3rd solution heat exchanger (11) and newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) or second condenser (15) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator and the 3rd solution heat exchanger, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, to divide steam chest (12) to have the concentrated solution pipeline to be communicated with first absorber (1) through second solution pump (7) is adjusted into branch steam chest (12) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through second solution pump (7) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with first absorber (1) through newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) or second condenser (15) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
57. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the concentrated solution pipeline to have the concentrated solution pipeline to be communicated with newly-increased absorber (L) with dividing steam chest (12) to be communicated with to be adjusted into second generator (5) in second generator (5) through second solution heat exchanger (10) through second solution heat exchanger (10) and absorption-generator (3), newly-increased absorber (L) also has the weak solution pipeline to be communicated with dividing steam chest (12) through newly-increased solution heat exchanger (C) and absorption-generator (3), to absorb-generator (3) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through the 3rd solution pump (8), newly-increased solution heat exchanger (C) and second solution heat exchanger (10) are communicated with second absorber (2), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, first generator (4) there is the concentrated solution pipeline through first solution heat exchanger (9), second solution heat exchanger (10) and absorption-generator (3) have the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9) and second solution heat exchanger (10) with dividing steam chest (12) to be communicated with to be adjusted into first generator (4), newly-increased absorber (L) also has the weak solution pipeline to be communicated with dividing steam chest (12) through newly-increased solution heat exchanger (C) and absorption-generator (3), to absorb-generator (3) has the weak solution pipeline to be communicated with second absorber (2) through the 3rd solution pump (8) and second solution heat exchanger (10) to be adjusted into absorption-generator (3) and the weak solution pipeline to be arranged through the 3rd solution pump (8), newly-increased solution heat exchanger (C) and second solution heat exchanger (10) are communicated with second absorber (2), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
58. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, when 1. second generator is arranged, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10) in second generator (5) is adjusted into second generator (5) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through second solution heat exchanger (10), newly-increased absorber (L) also has the weak solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C), to absorb-generator (3) has weak solution pipeline the 3rd solution pump (8) and is communicated with second absorber (2) through second solution heat exchanger (10) and be adjusted into absorption-generator (3) and the weak solution pipeline arranged through the 3rd solution pump (8), newly-increased solution heat exchanger (C) and second solution heat exchanger (10) are communicated with second absorber (2), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L); When 2. not having second generator, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with absorption-generator (3) through first solution heat exchanger (9) and second solution heat exchanger (10) in first generator (4) is adjusted into first generator (4) and has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through first solution heat exchanger (9) and second solution heat exchanger (10), newly-increased absorber (L) also has the weak solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C), to absorb-generator (3) has weak solution pipeline the 3rd solution pump (8) and is communicated with second absorber (2) through second solution heat exchanger (10) and be adjusted into absorption-generator (3) and the weak solution pipeline arranged through the 3rd solution pump (8), newly-increased solution heat exchanger (C) and second solution heat exchanger (10) are communicated with second absorber (2), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L).
59. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-6, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with absorption-generator (3) through second solution heat exchanger (10) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through second solution heat exchanger (10) and newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
60. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 7, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, there is the weak solution pipeline to have the weak solution pipeline to be communicated with newly-increased absorber (L) with dividing steam chest (12) to be communicated with to be adjusted into second absorber (2) second absorber (2) through second solution heat exchanger (10) and newly-increased solution heat exchanger (C) through second solution heat exchanger (10) and absorption-generator (3), newly-increased absorber (L) also has the weak solution pipeline to be communicated with dividing steam chest (12) through newly-increased solution heat exchanger (C) and absorption-generator (3), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) or second condenser (15) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
61. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 8-9, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline through first solution pump (6), newly-increased solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), with first absorber (1) have heated medium pipeline and external communications be adjusted into first evaporimeter (16) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber.
62. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 10, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the weak solution pipeline to be communicated with first generator (4) through first solution pump (6) and first solution heat exchanger (9) second absorber (2) is adjusted into second absorber (2) and has the weak solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased absorber (L) also has the weak solution pipeline through first solution pump (6), newly-increased solution heat exchanger (C) and first solution heat exchanger (9) are communicated with first generator (4), with first absorber (1) have heated medium pipeline and external communications be adjusted into second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), or be adjusted into first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L), newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first absorber; Wherein, when not having second evaporimeter, with second evaporimeter (17) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (K) and first absorber (1) after first absorber (1) is communicated with have the refrigerant vapour passage to be communicated with again to be adjusted into newly-increased absorber (L) first evaporimeter (16) set up the cryogen liquid pipeline through increase cryogen liquid pump (K) newly and after first absorber (1) is communicated with first absorber (1) have the refrigerant vapour passage to be communicated with again with newly-increased absorber (L).
63. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-10, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, first generator (4) had the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into first generator (4) has the refrigerant vapour passage to be communicated with newly-increased absorber (L), newly-increased absorber (L) has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first condenser (14), newly-increased generator (A) drives thermal medium pipeline and external communications in addition, newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by first generator.
64. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-10, increase newly-increased generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased choke valve, first generator (4) is set up the refrigerant vapour passage and is communicated with newly-increased absorber (L), newly-increased absorber (L) has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the refrigerant vapour passage to be communicated with newly-increased condenser (M), newly-increased condenser (M) also has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased choke valve (B), newly-increased generator (A) drives thermal medium pipeline and external communications in addition, newly-increased absorber (L) and newly-increased condenser (M) also have heated medium pipeline and external communications respectively, and formation is provided two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour respectively to first condenser and newly-increased absorber by first generator.
65. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-10, increase newly-increased generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorber (L), newly-increased absorber (L) has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the refrigerant vapour passage to be communicated with first absorber (1), newly-increased generator (A) drives thermal medium pipeline and external communications in addition, newly-increased absorber (L) also has heated medium pipeline and external communications, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber by newly-increased generator.
66. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 65, increase newly-increased condenser and newly-increased choke valve, newly-increased generator (A) is set up the refrigerant vapour passage and is communicated with newly-increased condenser (M), newly-increased condenser (M) also has the newly-increased choke valve (B) of cryogen liquid pipeline warp with first evaporimeter (16) connected sum heated medium pipeline and external communications to be arranged respectively, forms by newly-increased generator and provides two-stage multiterminal heat supply the 3rd class absorption heat pump of refrigerant vapour to increasing the condenser and first absorber newly respectively.
67. multiterminal heat supply the 3rd class absorption heat pump, be at claim 5-6, in described multiterminal heat supply the 3rd class absorption heat pump of 8-9, increase newly-increased choke valve or newly-increased cryogen liquid pump, newly-increased generator, newly-increased absorption-evaporimeter, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), newly-increased absorption-evaporimeter (J) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through newly-increased solution heat exchanger (C), first evaporimeter (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, or first condenser (14) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (J) newly after newly-increased absorption-evaporimeter (J) is communicated with and have the refrigerant vapour passage to be communicated with again with first absorber (1), newly-increased generator (A) also has refrigerant vapour passage and first absorber (1) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber jointly by newly-increased generator and newly-increased absorption-evaporimeter.
68. multiterminal heat supply the 3rd class absorption heat pump, be in claim 7, in 10 described multiterminal heat supply the 3rd class absorption heat pumps, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased absorption-evaporimeter, newly-increased solution pump and newly-increased solution heat exchanger, first evaporimeter (16) had the refrigerant vapour passage to be communicated with first absorber (1) to be adjusted into first evaporimeter (16) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (J), newly-increased absorption-evaporimeter (J) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorption-evaporimeter (J) through newly-increased solution heat exchanger (C), first evaporimeter (16) or second condenser (15) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing cryogen liquid pump (K) newly and newly-increased absorption-evaporimeter (J) is communicated with has the refrigerant vapour passage to be communicated with first absorber (1) again, newly-increased generator (A) also has refrigerant vapour passage and first absorber (1) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, forms two-stage multiterminal heat supply the 3rd class absorption heat pump that refrigerant vapour is provided to first absorber jointly by newly-increased generator and newly-increased absorption-evaporimeter; Wherein, when not having second evaporimeter, also can select to increase newly-increased choke valve and set up cryogen liquid pipeline newly-increased absorption-evaporimeter (J) after increasing choke valve (B) newly and newly-increased absorption-evaporimeter (J) is communicated with by first condenser (14) has the refrigerant vapour passage to be communicated with first absorber (1) again.
69. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage economic benefits and social benefits of claim 11-23 multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase generator (A) newly has the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into newly-increased generator (A) and has the refrigerant vapour passage to be communicated with newly-increased absorber (L), newly-increased absorber (L) has the weak solution pipeline to be communicated with newly-increased second generator (F) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased second generator (F) also has refrigerant vapour passage and first condenser (14) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased absorber (L) also has heated medium pipeline and external communications, and forming with the single-stage economic benefits and social benefits is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
70. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 69, increase newly-increased the 3rd choke valve, to increase second generator (F) newly has and drives thermal medium pipeline and external communications and be adjusted into first generator (4) and set up the refrigerant vapour passage and is communicated with the back with newly-increased second generator (F) and increases second generator (F) newly and have cryogen liquid pipeline warp to increase the 3rd choke valve newly again to be communicated with first condenser (14), and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage economic benefits and social benefits.
71. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage economic benefits and social benefits of claim 11-23 multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased second generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the 3rd choke valve, newly-increased generator (A) is set up the refrigerant vapour passage and is communicated with newly-increased absorber (L), newly-increased absorber (L) has the weak solution pipeline to be communicated with newly-increased second generator (F) through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased second generator (F) also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased second generator (F) also has refrigerant vapour passage and newly-increased condenser (M) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased condenser (M) also has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased the 3rd choke valve (G), newly-increased absorber (L) and newly-increased condenser (M) also have heated medium pipeline and external communications respectively, and forming with the single-stage economic benefits and social benefits is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
72. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 71, increase newly-increased the 4th choke valve, to increase second generator (F) newly has and drives thermal medium pipeline and external communications and be adjusted into first generator (4) and set up the refrigerant vapour passage and is communicated with the back with newly-increased second generator (F) and increases second generator (F) newly and have cryogen liquid pipeline warp to increase the 4th choke valve newly again to be communicated with newly-increased condenser (M), and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage economic benefits and social benefits.
73. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage triple effect of claim 24-38 multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase second generator (F) newly has the refrigerant vapour passage to be communicated with first condenser (14) to be adjusted into newly-increased second generator (F) to have the refrigerant vapour passage to be communicated with newly-increased absorber (L), newly-increased absorber (L) also has the weak solution pipeline to be communicated with newly-increased the 3rd generator through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased the 3rd generator also has refrigerant vapour passage and first condenser (14) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased absorber (L) also has heated medium pipeline and external communications, and forming with the single-stage triple effect is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
74. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 73, increase newly-increased the 4th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into newly-increased first generator (A) and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 4th choke valve newly again to be communicated with first condenser (14), and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
75. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 73, increase newly-increased the 4th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into first generator (4) and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 4th choke valve newly again to be communicated with first condenser (14), and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
76. multiterminal heat supply the 3rd class absorption heat pump, be in the described single-stage triple effect of claim 21-31 multiterminal heat supply the 3rd class absorption heat pump, increase newly-increased the 3rd generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the 4th choke valve, newly-increased second generator (F) is set up the refrigerant vapour passage and is communicated with newly-increased absorber (L), newly-increased absorber (L) also has the weak solution pipeline to be communicated with newly-increased the 3rd generator through newly-increased solution pump (E) and newly-increased solution heat exchanger (C), newly-increased the 3rd generator also has the concentrated solution pipeline to be communicated with newly-increased absorber (L) through newly-increased solution heat exchanger (C), newly-increased the 3rd generator also has refrigerant vapour passage and newly-increased condenser (M) connected sum that the thermal medium pipeline of driving and external communications are arranged respectively, newly-increased condenser (M) also has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased the 4th choke valve, newly-increased absorber (L) and newly-increased condenser (M) also have heated medium pipeline and external communications respectively, and forming with the single-stage triple effect is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order.
77. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 76, increase newly-increased the 5th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into newly-increased first generator (A) and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 5th choke valve newly again to be communicated with newly-increased condenser (M), and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
78. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 76, increase newly-increased the 5th choke valve, to increase the 3rd generator newly has and drives thermal medium pipeline and external communications and be adjusted into first generator (4) and set up the refrigerant vapour passage and is communicated with the back with newly-increased the 3rd generator and increases the 3rd generator newly and have cryogen liquid pipeline warp to increase the 5th choke valve newly again to be communicated with newly-increased condenser (M), and formation is two-stage multiterminal heat supply the 3rd class absorption heat pump of the first order with the single-stage triple effect.
79. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 11-38, increase newly-increased condenser and newly-increased the 4th choke valve, first generator (4) is set up the refrigerant vapour passage and is communicated with newly-increased condenser (M), newly-increased condenser (M) also has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased the 4th choke valve (P), newly-increased condenser (M) also has heated medium pipeline and external communications, forms with multiterminal heat supply three class absorption heat pump of newly-increased condenser for additional high-temperature heat supply end.
80. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 24-38, increase newly-increased condenser and newly-increased the 4th choke valve, newly-increased first generator (A) is set up the refrigerant vapour passage and is communicated with newly-increased condenser (M), newly-increased condenser (M) also has the cryogen liquid pipeline to be communicated with first condenser (14) through newly-increased the 4th choke valve (P), newly-increased condenser (M) also has heated medium pipeline and external communications, forms with multiterminal heat supply three class absorption heat pump of newly-increased condenser for additional high-temperature heat supply end.
81. multiterminal heat supply the 3rd class absorption heat pump, be in described multiterminal heat supply the 3rd class absorption heat pump of claim 5-62, increase the first flow control valve and second flow control valve, with first condenser (14) have heated medium pipeline and external communications be adjusted into the outside have the heated medium pipeline be communicated with first condenser (14) back first condenser (14) have the heated medium pipeline to be communicated with second absorber (2) with external communications with through second flow control valve (O) through first flow choke valve (N) respectively again, having heated medium pipeline and external communications to be adjusted into first condenser (14) second absorber (2) has heated medium pipeline second absorber (2) after the second flow choke valve (O) and second absorber (2) and external communications that heated medium pipeline and external communications are arranged again, forms adjustable type multiterminal heat supply the 3rd class absorption heat pump.
CN2010106124989A 2010-12-18 2010-12-18 Backheating type absorption-generation system and multiterminal heat-supply third-class absorption heat pump Pending CN102042712A (en)

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CN103697615A (en) * 2013-12-07 2014-04-02 李华玉 Multi-end heat supply class-III absorptive heat pump
CN103697615B (en) * 2013-12-07 2016-05-04 李华玉 Multiterminal heat supply the 3rd class absorption heat pump
CN104807238A (en) * 2014-03-24 2015-07-29 李华玉 Absorption heat pump of fourth class and absorption heat pump of fifth class
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