CN102072583B - Regenerative absorption-generation system and regenerative third-type absorption heat pump - Google Patents

Regenerative absorption-generation system and regenerative third-type absorption heat pump Download PDF

Info

Publication number
CN102072583B
CN102072583B CN2010106219230A CN201010621923A CN102072583B CN 102072583 B CN102072583 B CN 102072583B CN 2010106219230 A CN2010106219230 A CN 2010106219230A CN 201010621923 A CN201010621923 A CN 201010621923A CN 102072583 B CN102072583 B CN 102072583B
Authority
CN
China
Prior art keywords
newly
increased
communicated
generator
absorption
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN2010106219230A
Other languages
Chinese (zh)
Other versions
CN102072583A (en
Inventor
李华玉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN2010106219230A priority Critical patent/CN102072583B/en
Publication of CN102072583A publication Critical patent/CN102072583A/en
Application granted granted Critical
Publication of CN102072583B publication Critical patent/CN102072583B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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 a regenerative absorption-generation system and a regenerative third-type absorption heat pump, belongs to the technical field of absorption heat pumps. The regenerative absorption-generation system is formed by taking an absorption evaporator, an absorber, a first absorption-generator, a second absorption-generator, a generator, a plurality of solution pumps, a plurality of solution heat exchangers, a first steam distributing chamber, a second steam distributing chamber or a solution throttle valve as main components, adopting a single-way solution circulation or adopting a dual-way solution circulation, forming a heat return flow by an absorption-evaporator, the first absorption-generator and the second steam distributing chamber, forming a solution generation flow which relays on second-type driving force by the second absorption-evaporator and the first steam distributing chamber, and forming the solution generation flow which relays on first-type driving force by the generator. Regenerative absorption-generation system-based full range of regenerative third-type absorption heat pumps are formed by adding other related components including a first condenser, a second condenser and a first evaporator or adding a second evaporator, a throttle valve and a cold agent liquid pump into the regenerative absorption-generation system.

Description

Backheating type absorption-generation systems and back-heating type the 3rd class absorption heat pump
Technical field:
The invention belongs to the low temperature heat 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 larger 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 residual heat resources of lower temperature, key is to improve the weak solution concentration of absorber outlet.Take rational technical measures, improve simultaneously the weak solution concentration of absorber outlet and reduce the solution concentration that enters generator, and the amplitude that can select according to demand within the specific limits solution concentration to reduce and improve, this will have very important meaning.
For the heat supply temperature that promotes the 3rd class absorption heat pump, make it have higher performance index and realize between the running parameter and the free of discontinuities between the performance index is connected, the present invention adopts cleverly flow process, with the absorption-generating process of backheat application of principle in solution, consist of the backheat flow process with absorption-evaporimeter and the first absorption-generator, set up backheating type absorption-generation systems; And take backheating type absorption-generation systems as the basis, increase the associated components that comprises the first condenser, the second condenser, the first evaporimeter or add the second evaporimeter, choke valve and cryogen liquid pump, obtain back-heating type the 3rd class absorption heat pump of different effect numbers, different progression, make each running parameter interval that the 3rd corresponding class absorption heat pump be arranged, 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 backheating type absorption-generation systems and back-heating type the 3rd class absorption heat pump, comprises four kinds of backheating type absorption-generation systems and a series of back-heating type the 3rd class absorption heat pump based on backheating type absorption-generation systems.Concrete summary of the invention subitem is described below:
1. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest and second minute steam chest form, absorption-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump, the first absorption-generator also has the weak solution pipeline to be communicated with first minute steam chest through the second solution heat exchanger and the second absorption-generator, steam chest also had the concentrated solution pipeline through the second solution pump in first minute, the second solution heat exchanger and the first absorption-generator are communicated with second minute steam chest, steam chest also had the concentrated solution pipeline to be communicated with absorber in second minute, absorber also has the weak solution pipeline to be communicated with absorption-evaporimeter, the second absorption-generator has the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger, generator also has the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger, absorption-evaporimeter also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter had the refrigerant vapour passage to be communicated with the first absorption-generator again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter, absorber also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, steam chest also had the refrigerant vapour passage to be communicated with absorption-evaporimeter in second minute, first minute steam chest also has the refrigerant vapour passage to be communicated with or also to have respectively refrigerant vapour passage and outside connected sum to have the cooling medium pipeline to be communicated with the outside with outside, the second absorption-generator also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms two-way and loops back hot type absorption-generation systems; Wherein, or adopt the solution choke valve to replace the second solution heat exchanger, having the weak solution pipeline to be communicated with first minute steam chest through the second solution heat exchanger and the second absorption-generator in the first absorption-generator changes to the first absorption-generator and has the weak solution pipeline to be communicated with first minute steam chest through solution choke valve and the second absorption-generator, first minute steam chest had the concentrated solution pipeline through the second solution pump, the second solution heat exchanger and the first absorption-generator are communicated with second minute steam chest and change to first minute steam chest and have the concentrated solution pipeline to be communicated with second minute steam chest through the second solution pump and the first absorption-generator.
2. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest, second minute steam chest, the 4th solution pump and solution choke valve form, absorption-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump, the first absorption-generator also has the weak solution pipeline to be communicated with first minute steam chest through the second solution heat exchanger and the second absorption-generator, steam chest also had the concentrated solution pipeline through the second solution pump in first minute, the second solution heat exchanger and the first absorption-generator are communicated with second minute steam chest, steam chest also had the concentrated solution pipeline to be communicated with absorber through the 4th solution pump in second minute, absorber also has the weak solution pipeline to be communicated with absorption-evaporimeter through the solution choke valve, the second absorption-generator has the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger, generator also has the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger, absorption-evaporimeter also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter had the refrigerant vapour passage to be communicated with the first absorption-generator again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter, absorber also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, steam chest also had the refrigerant vapour passage to be communicated with absorption-evaporimeter in second minute, first minute steam chest also has the refrigerant vapour passage to be communicated with or also to have respectively refrigerant vapour passage and outside connected sum to have the cooling medium pipeline to be communicated with the outside with outside, the second absorption-generator also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms two-way and loops back hot type absorption-generation systems; Wherein, or adopt the second solution choke valve to replace the second solution heat exchanger, having the weak solution pipeline to be communicated with first minute steam chest through the second solution heat exchanger and the second absorption-generator in the first absorption-generator changes to the first absorption-generator and has the weak solution pipeline to be communicated with first minute steam chest through the second solution choke valve and the second absorption-generator, first minute steam chest had the concentrated solution pipeline through the second solution pump, the second solution heat exchanger and the first absorption-generator are communicated with second minute steam chest and change to first minute steam chest and have the concentrated solution pipeline to be communicated with second minute steam chest through the second solution pump and the first absorption-generator.
3. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest and second minute steam chest form, absorption-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump, the first absorption-generator also has the weak solution pipeline to be communicated with the second absorption-generator through the second solution heat exchanger, the second absorption-generator also has the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger, generator also has the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator, steam chest also had the concentrated solution pipeline through the second solution pump in first minute, the second solution heat exchanger and the first absorption-generator are communicated with second minute steam chest, steam chest also had the concentrated solution pipeline to be communicated with absorber in second minute, absorber also has the weak solution pipeline to be communicated with absorption-evaporimeter, absorption-evaporimeter also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter had the refrigerant vapour passage to be communicated with the first absorption-generator again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter, absorber also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, steam chest also had the refrigerant vapour passage to be communicated with absorption-evaporimeter in second minute, steam chest also had the refrigerant vapour passage to be communicated with outside in first minute, the second absorption-generator also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms single channel and loops back hot type absorption-generation systems; Wherein, or adopt the solution choke valve to replace the second solution heat exchanger, there is the weak solution pipeline to be communicated with the second absorption-generator through the second solution heat exchanger in the first absorption-generator and changes to the first absorption-generator and have the weak solution pipeline to be communicated with the second absorption-generator through the solution choke valve, have the concentrated solution pipeline to be communicated with second minute steam chest through the second solution pump, the second solution heat exchanger and the first absorption-generator first minute steam chest and change to first minute steam chest and have the concentrated solution pipeline to be communicated with second minute steam chest through the second solution pump and the first absorption-generator.
4. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest, second minute steam chest, the 4th solution pump and solution choke valve form, absorption-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump, the first absorption-generator also has the weak solution pipeline to be communicated with the second absorption-generator through the second solution heat exchanger, the second absorption-generator also has the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger, generator also has the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator, steam chest also had the concentrated solution pipeline through the second solution pump in first minute, the second solution heat exchanger and the first absorption-generator are communicated with second minute steam chest, steam chest also had the concentrated solution pipeline to be communicated with absorber through the 4th solution pump in second minute, absorber also has the weak solution pipeline to be communicated with absorption-evaporimeter through the solution choke valve, absorption-evaporimeter also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter had the refrigerant vapour passage to be communicated with the first absorption-generator again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter, absorber also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, steam chest also had the refrigerant vapour passage to be communicated with absorption-evaporimeter in second minute, steam chest also had the refrigerant vapour passage to be communicated with outside in first minute, the second absorption-generator also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms single channel and loops back hot type absorption-generation systems; Wherein, or adopt the second solution choke valve to replace the second solution heat exchanger, there is the weak solution pipeline to be communicated with the second absorption-generator through the second solution heat exchanger in the first absorption-generator and changes to the first absorption-generator and have the weak solution pipeline to be communicated with the second absorption-generator through the second solution choke valve, have the concentrated solution pipeline to be communicated with second minute steam chest through the second solution pump, the second solution heat exchanger and the first absorption-generator first minute steam chest and change to first minute steam chest and have the concentrated solution pipeline to be communicated with second minute steam chest through the second solution pump and the first absorption-generator.
5. back-heating type the 3rd class absorption heat pump, in the 1st described backheating type absorption-generation systems, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, choke valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through choke valve, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorption-generator in the second absorption-generator, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser first minute steam chest, the second condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump, to absorb-evaporimeter has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorber absorber, absorption-evaporimeter has the refrigerant vapour passage to be communicated with the first absorption-generator to be defined as the first evaporimeter or the second condenser to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter the outside, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein, during without the second evaporimeter, the first condenser has the cryogen liquid pipeline to be communicated with the second evaporimeter through choke valve to change to the first condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through choke valve, and the first evaporimeter increases the refrigerant vapour passage and is communicated with the second absorption-generator.
6. back-heating type the 3rd class absorption heat pump, in the 2nd described backheating type absorption-generation systems, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the second choke valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorption-generator in the second absorption-generator, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser first minute steam chest, the second condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump, the first evaporimeter also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the second choke valve, to absorb-evaporimeter has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorber absorber, absorption-evaporimeter has the refrigerant vapour passage to be communicated with the first absorption-generator to be defined as the 3rd evaporimeter or the first evaporimeter to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter the outside, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter, the second evaporimeter and the 3rd evaporimeter medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein, during without the second evaporimeter, the first condenser has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve to change to the first condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve, and the first evaporimeter increases the refrigerant vapour passage and is communicated with the second absorption-generator.
7. back-heating type the 3rd class absorption heat pump, described at the 3rd, the second absorption-generator has in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the first cryogen liquid pump, the second cryogen liquid pump or the 3rd choke valve, first throttle valve and the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser first minute steam chest, the second condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter or the second evaporimeter through the first cryogen liquid pump, the first evaporimeter also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorption-generator in the second absorption-generator, to absorb-evaporimeter has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorber absorber, absorption-evaporimeter has the refrigerant vapour passage to be communicated with the first absorption-generator to be defined as the first evaporimeter to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter the outside, or be defined as the first condenser and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator through the 3rd choke valve with absorption-evaporimeter after absorption-evaporimeter is communicated with, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: during 1. without the second evaporimeter, the second condenser has the cryogen liquid pipeline to be communicated with the first evaporimeter or the second evaporimeter through the first cryogen liquid pump to be defined as the second condenser and to have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump, cancel the cryogen liquid pipeline that the first evaporimeter is communicated with the second evaporimeter through the second choke valve, the first evaporimeter increases the refrigerant vapour passage and is communicated with the second absorption-generator; 2. or have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve the first condenser to be adjusted into the first condenser and to have the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve, simultaneously the first evaporimeter being had the cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve is adjusted into the second evaporimeter and has the cryogen liquid pipeline to be communicated with the first evaporimeter through the second choke valve.
8. back-heating type the 3rd class absorption heat pump, described at the 3rd, the second absorption-generator is without in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the first cryogen liquid pump, the first throttle valve, the second cryogen liquid pump or the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser first minute steam chest, the second condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorption-generator in the second absorption-generator, to absorb-evaporimeter has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorber absorber, absorption-evaporimeter has the refrigerant vapour passage to be communicated with the first absorption-generator to be defined as the first evaporimeter to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter the outside, or be defined as the first condenser and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator through the second choke valve with absorption-evaporimeter after absorption-evaporimeter is communicated with, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter and the second evaporimeter medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: 1. or increase by the 3rd choke valve, the first evaporimeter increases the cryogen liquid pipeline and is communicated with the second evaporimeter through the 3rd choke valve, the second condenser is had the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump again and changes to the second condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump; During 2. without the second evaporimeter, the second condenser has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump to change to the second condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump, and the first evaporimeter increases the refrigerant vapour passage and is communicated with the second absorption-generator.
9. back-heating type the 3rd class absorption heat pump, described at the 4th, the second absorption-generator has in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the first cryogen liquid pump, the second choke valve, the 3rd choke valve, the second cryogen liquid pump or the 4th choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve, the second evaporimeter also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the 3rd choke valve, the first evaporimeter also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser first minute steam chest, the second condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorption-generator in the second absorption-generator, to absorb-evaporimeter has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorber absorber, absorption-evaporimeter has the refrigerant vapour passage to be communicated with the first absorption-generator to be defined as the first evaporimeter or the second evaporimeter to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter the outside, or be defined as the first condenser and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator through the 4th choke valve with absorption-evaporimeter after absorption-evaporimeter is communicated with, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter, the second evaporimeter and the 3rd evaporimeter medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: 1. or with the first condenser have the cryogen liquid pipeline to be communicated with the second evaporimeter through the first throttle valve, the second evaporimeter has the cryogen liquid pipeline to be communicated with the first evaporimeter through the 3rd choke valve to change to the first condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve again, the first evaporimeter or the 3rd evaporimeter have the cryogen liquid pipeline to be communicated with the second evaporimeter through the 3rd choke valve, have the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump the second condenser and change to the second condenser and have the cryogen liquid pipeline to be communicated with the second evaporimeter or the first evaporimeter through the first cryogen liquid pump; During 2. without the second evaporimeter, the second condenser has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump to change to the second condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump, the first condenser have the cryogen liquid pipeline through the first throttle valve be communicated with the second evaporimeter, the second evaporimeter has the cryogen liquid pipeline to be communicated with the first evaporimeter through the 3rd choke valve to change to the first condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve again, the first evaporimeter increases the refrigerant vapour passage and is communicated with the second absorption-generator.
10. back-heating type the 3rd class absorption heat pump, described at the 4th, the second absorption-generator is without in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the first cryogen liquid pump, the second choke valve, the second cryogen liquid pump or the 3rd choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator and to have the refrigerant vapour passage to be communicated with the first condenser in generator, the first condenser also has the cryogen liquid pipeline to be communicated with the first evaporimeter through the first throttle valve, the first evaporimeter also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter through the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest and to have the refrigerant vapour passage to be communicated with the second condenser first minute steam chest, the second condenser also has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter and to have the refrigerant vapour passage to be communicated with the second absorption-generator in the second absorption-generator, to absorb-evaporimeter has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter and to have the refrigerant vapour passage to be communicated with absorber absorber, absorption-evaporimeter has the refrigerant vapour passage to be communicated with the first absorption-generator to be defined as the first evaporimeter to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator through the second cryogen liquid pump with absorption-evaporimeter after absorption-evaporimeter is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter the outside, or be defined as the first condenser and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator through the 3rd choke valve with absorption-evaporimeter after absorption-evaporimeter is communicated with, the first condenser also has the heated medium pipeline to be communicated with outside, the second condenser also has the cooling medium pipeline to be communicated with outside, the first evaporimeter, the second evaporimeter and the 3rd evaporimeter medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: 1. or increase by the 4th choke valve, the first evaporimeter or the 3rd evaporimeter increase the cryogen liquid pipeline and are communicated with the second evaporimeter through the 4th choke valve, simultaneously the second condenser are had the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump and change to the second condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump; During 2. without the second evaporimeter, the second condenser has the cryogen liquid pipeline to be communicated with the second evaporimeter through the first cryogen liquid pump to change to the second condenser and have the cryogen liquid pipeline to be communicated with the first evaporimeter through the first cryogen liquid pump, and the first evaporimeter increases the refrigerant vapour passage and is communicated with the second absorption-generator.
11. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 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 the second absorption-generator through newly-increased solution heat exchanger, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage parallel double-effect back-heating type the 3rd class absorption heat pump.
12. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-10 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 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 generator after the first solution heat exchanger after newly-increased solution heat exchanger, be communicated with first minute steam chest through the second absorption-generator again, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage parallel double-effect back-heating type the 3rd class absorption heat pump.
13. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger in generator is adjusted into 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 the second absorption-generator through the first solution heat exchanger, having the weak solution pipeline to be communicated with generator through the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with generator through the first solution heat exchanger and newly-increased solution heat exchanger, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
14. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-10 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator in generator is adjusted into 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 first minute steam chest through the first solution heat exchanger and the second absorption-generator, having the weak solution pipeline to be communicated with generator through the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with generator through the first solution heat exchanger and newly-increased solution heat exchanger, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
15. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 13-14 item, having the weak solution pipeline to be communicated with generator through the first solution pump, the first solution heat exchanger and newly-increased solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with generator through newly-increased solution heat exchanger with newly-increased generator connected sum respectively directly after the first solution pump and the first solution heat exchanger again, formation single-stage connection in series-parallel economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
16. back-heating type the 3rd class absorption heat pump, in described back-heating type 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, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased generator through the first solution pump and the first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger in generator is adjusted into generator and has the concentrated solution pipeline to be communicated with the second absorption-generator through newly-increased solution heat exchanger and the first solution heat exchanger, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
17. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-10 item, 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 generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased generator through the first solution pump and the first solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator in generator is adjusted into generator and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger, the first solution heat exchanger and the second absorption-generator are communicated with first minute steam chest, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
18. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 16-17 item, having the weak solution pipeline to be communicated with newly-increased generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased generator and generator respectively after the first solution pump and the first solution heat exchanger, form single-stage connection in series-parallel economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
19. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, the first solution pump is set up the weak solution pipeline and is communicated with newly-increased the second generator through newly-increased the second solution heat exchanger with newly-increased generator connected sum through newly-increased solution heat exchanger respectively, newly-increased generator also has the concentrated solution pipeline to be communicated with the second absorption-generator through newly-increased solution heat exchanger, newly-increased the second generator also has the concentrated solution pipeline to be communicated with the second absorption-generator through newly-increased the second solution heat exchanger, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator had newly-increased the second choke valve of cryogen liquid pipeline warp to be communicated with the first condenser again after newly-increased generator also had refrigerant vapour passage and newly-increased the second generator to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, newly-increased the second generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage triple effect back-heating type in parallel the 3rd class absorption heat pump.
20. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-10 item, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, the first solution pump is set up the weak solution pipeline and is communicated with newly-increased the second generator through newly-increased the second solution heat exchanger with newly-increased generator connected sum through newly-increased solution heat exchanger respectively, newly-increased generator has the concentrated solution pipeline through having the concentrated solution pipeline all to converge with the concentrated solution pipeline of generator after the first solution heat exchanger with newly-increased the second generator after the newly-increased solution heat exchanger after newly-increased the second solution heat exchanger, be communicated with first minute steam chest through the second absorption-generator again, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator had newly-increased the second choke valve of cryogen liquid pipeline warp to be communicated with the first condenser again after newly-increased generator also had refrigerant vapour passage and newly-increased the second generator to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, newly-increased the second generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage triple effect back-heating type in parallel the 3rd class absorption heat pump.
21. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, having the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger in generator is adjusted into generator and has the concentrated solution pipeline to be communicated with newly-increased generator through the first solution heat exchanger, newly-increased generator also has the newly-increased solution heat exchanger of concentrated solution pipeline to be communicated with newly-increased the second generator, newly-increased the second generator also has the concentrated solution pipeline to be communicated with the second absorption-generator through newly-increased the second solution heat exchanger, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and the weak solution pipeline is arranged through the first solution pump, newly-increased the second solution heat exchanger, newly-increased solution heat exchanger and the first solution heat exchanger are communicated with generator, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator had newly-increased the second choke valve of cryogen liquid pipeline warp to be communicated with the first condenser again after newly-increased generator also had refrigerant vapour passage and newly-increased the second generator to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, newly-increased the second generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
22. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-10 item, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, having the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator in generator is adjusted into generator and has the concentrated solution pipeline to be communicated with newly-increased generator through the first solution heat exchanger, newly-increased generator also has the newly-increased solution heat exchanger of concentrated solution pipeline to be communicated with newly-increased the second generator, newly-increased the second generator also has the concentrated solution pipeline to be communicated with first minute steam chest through newly-increased the second solution heat exchanger and the second absorption-generator, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and the weak solution pipeline is arranged through the first solution pump, newly-increased the second solution heat exchanger, newly-increased solution heat exchanger and the first solution heat exchanger are communicated with generator, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator had newly-increased the second choke valve of cryogen liquid pipeline warp to be communicated with the first condenser again after newly-increased generator also had refrigerant vapour passage and newly-increased the second generator to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, newly-increased the second generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
23. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-6 item, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased solution pump and newly-increased the second solution pump, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased the second generator through the first solution pump and the first solution heat exchanger, newly-increased the second generator also has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased the second solution pump and newly-increased the second solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger in generator is adjusted into generator and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger, newly-increased the second solution heat exchanger and the first solution heat exchanger are communicated with the second absorption-generator, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator had newly-increased the second choke valve of cryogen liquid pipeline warp to be communicated with the first condenser again after newly-increased generator also had refrigerant vapour passage and newly-increased the second generator to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, newly-increased the second generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
24. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-10 item, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased solution pump and newly-increased the second solution pump, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased the second generator through the first solution pump and the first solution heat exchanger, newly-increased the second generator also has the concentrated solution pipeline to be communicated with newly-increased generator through newly-increased the second solution pump and newly-increased the second solution heat exchanger, newly-increased generator also has the concentrated solution pipeline to be communicated with generator through newly-increased solution pump and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator in generator is adjusted into generator and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, the first solution heat exchanger and the second absorption-generator are communicated with first minute steam chest, newly-increased generator has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again after having the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator to have the refrigerant vapour passage to be communicated with newly-increased generator the generator---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator had newly-increased the second choke valve of cryogen liquid pipeline warp to be communicated with the first condenser again after newly-increased generator also had refrigerant vapour passage and newly-increased the second generator to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, newly-increased the second generator also has the refrigerant vapour passage to be communicated with the first condenser, forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
25. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, to absorb-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump to be adjusted into absorption-evaporimeter and to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump and newly-increased solution heat exchanger, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first evaporimeter or the 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 absorption-evaporimeter and absorber respectively again, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
26. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorption-evaporimeter, to absorb-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump to be adjusted into absorption-evaporimeter and to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump and newly-increased solution heat exchanger, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the 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 absorption-evaporimeter and absorber respectively 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 again the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively, formation provides one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to absorber.
27. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, there is the weak solution pipeline to be communicated with absorption-evaporimeter to be adjusted into absorber to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger absorber, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with absorption-evaporimeter through newly-increased solution pump and newly-increased solution heat exchanger, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first evaporimeter or the 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 absorption-evaporimeter and absorber respectively again, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
28. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorption-evaporimeter, there is the weak solution pipeline to be communicated with absorption-evaporimeter to be adjusted into absorber to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger absorber, newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with absorption-evaporimeter through newly-increased solution pump and newly-increased solution heat exchanger, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the 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 absorption-evaporimeter and absorber respectively 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 again the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively, formation provides one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to absorber.
29. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter, newly-increased cryogen liquid pump and newly-increased solution pump, second minute steam chest had the concentrated solution pipeline to be communicated with absorber to be adjusted into second minute steam chest has the concentrated solution pipeline to be communicated with absorber through newly-increased solution pump and newly-increased solution heat exchanger, there is the weak solution pipeline to be communicated with absorption-evaporimeter to be adjusted into absorber to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger absorber, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with absorption-evaporimeter again, the first evaporimeter had the refrigerant vapour passage to be communicated with absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the first evaporimeter or the 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 absorber again, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
30. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased solution pump, second minute steam chest had the concentrated solution pipeline to be communicated with absorber to be adjusted into second minute steam chest has the concentrated solution pipeline to be communicated with absorber through newly-increased solution pump and newly-increased solution heat exchanger, there is the weak solution pipeline to be communicated with absorption-evaporimeter to be adjusted into absorber to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger absorber, newly-increased absorption-evaporimeter has the weak solution pipeline to be communicated with absorption-evaporimeter again, the first evaporimeter had the refrigerant vapour passage to be communicated with absorber to be adjusted into the first evaporimeter has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter, the 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 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 again the refrigerant vapour passage to be communicated with absorber, formation provides one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to absorber.
31. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, to absorb-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump to be adjusted into absorption-evaporimeter and to have the weak solution pipeline to be communicated with newly-increased absorber through the 3rd solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with the first absorption-generator through newly-increased solution heat exchanger, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter or the second condenser and to set up the cryogen liquid pipeline and have again the refrigerant vapour passage to be communicated with newly-increased absorber through increasing the cryogen liquid pump newly and increasing absorber newly after absorber is communicated with absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
32. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, to absorb-evaporimeter has the weak solution pipeline to be communicated with the first absorption-generator through the 3rd solution pump to be adjusted into absorption-evaporimeter and to have the weak solution pipeline to be communicated with newly-increased absorber through the 3rd solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with the first absorption-generator through newly-increased solution heat exchanger, there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter and to set up the cryogen liquid pipeline and have again the refrigerant vapour passage to be communicated with newly-increased absorber through increasing the cryogen liquid pump newly and increasing absorber newly after absorber is communicated with absorber, or be adjusted into the first condenser set up the cryogen liquid pipeline through newly-increased choke valve with increase absorber newly after absorber is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
33. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger in generator is adjusted into generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through the first solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with the second absorption-generator through newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and the weak solution pipeline is arranged through the first solution pump, newly-increased solution heat exchanger and the first solution heat exchanger are communicated with generator, with absorber have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, or be adjusted into that the first condenser is set up the cryogen liquid pipeline through newly-increased choke valve and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber; Wherein, when the second evaporimeter, the second evaporimeter the cryogen liquid pipeline is arranged through newly-increased cryogen liquid pump and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber to change to the first evaporimeter have the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber.
34. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator in generator is adjusted into generator and has the concentrated solution pipeline to be communicated with newly-increased absorber through the first solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with first minute steam chest through newly-increased solution heat exchanger and the second absorption-generator, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and the weak solution pipeline is arranged through the first solution pump, newly-increased solution heat exchanger and the first solution heat exchanger are communicated with generator, with absorber have the heated medium pipeline with outside is communicated be adjusted into the first evaporimeter have the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, or be adjusted into that the first condenser has the cryogen liquid pipeline through newly-increased choke valve and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
35. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger in generator is adjusted into generator and has the concentrated solution pipeline to be communicated with the second absorption-generator through the first solution heat exchanger and newly-increased solution heat exchanger, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with generator through newly-increased solution pump and the first solution heat exchanger, with absorber have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, or be adjusted into that the first condenser is set up the cryogen liquid pipeline through newly-increased choke valve and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber; Wherein, when the second evaporimeter, the second evaporimeter the cryogen liquid pipeline is arranged through newly-increased cryogen liquid pump and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber to change to the first evaporimeter have the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber.
36. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with first minute steam chest through the first solution heat exchanger and the second absorption-generator in generator is adjusted into generator and the concentrated solution pipeline is arranged through the first solution heat exchanger, newly-increased solution heat exchanger and the second absorption-generator are communicated with first minute steam chest, having the weak solution pipeline to be communicated with generator through the first solution pump and the first solution heat exchanger in the second absorption-generator is adjusted into the second absorption-generator and has the weak solution pipeline to be communicated with newly-increased absorber through the first solution pump and newly-increased solution heat exchanger, newly-increased absorber also has the weak solution pipeline to be communicated with generator through newly-increased solution pump and the first solution heat exchanger, with absorber have the heated medium pipeline with outside is communicated be adjusted into the first evaporimeter have the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, or be adjusted into that the first condenser has the cryogen liquid pipeline through newly-increased choke valve and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
37. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-10 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator has 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 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 respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by generator.
38. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 5-10 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorber, newly-increased condenser and newly-increased choke valve, 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 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 the first condenser through newly-increased choke valve, newly-increased generator drives in addition the thermal medium pipeline and is communicated with outside, newly-increased absorber and newly-increased condenser also have respectively the heated medium pipeline to be communicated with outside, and formation is provided respectively double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour to the first condenser and newly-increased absorber by generator.
39. back-heating type the 3rd class absorption heat pump, the 5th, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the first evaporimeter has 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 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 absorption-evaporimeter and absorber respectively, newly-increased generator drives in addition the thermal medium pipeline and is communicated with outside, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms by increasing generator newly to absorber or double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour being provided to absorber and absorption-evaporimeter.
40. back-heating type the 3rd class absorption heat pump, in the 39th described back-heating type 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 to be communicated with the first evaporimeter through newly-increased choke valve, newly-increased condenser also has the heated medium pipeline to be communicated with outside, formation by newly-increased generator respectively to newly-increased condenser and absorber or to newly-increased condenser, absorber and absorption-evaporimeter provide double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour.
41. back-heating type the 3rd class absorption heat pump, described at the 5th, absorption-evaporimeter and the second absorption-generator are without in heated medium pipeline and outside back-heating type the 3rd class absorption heat pump that is communicated with, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator has 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 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, with absorber have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, or be adjusted into that the first condenser is set up the cryogen liquid pipeline through newly-increased choke valve and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased generator also has respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber jointly by absorber and generator; Wherein, when the second evaporimeter, the second evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber to change to the first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber.
42. back-heating type the 3rd class absorption heat pump, described at the 8th, absorption-evaporimeter is without in heated medium pipeline and outside back-heating type the 3rd class absorption heat pump that is communicated with, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator had the refrigerant vapour passage to be communicated with the first condenser to be adjusted into generator has 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 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, with absorber have the heated medium pipeline with outside is communicated be adjusted into the first evaporimeter set up the cryogen liquid pipeline through increase the cryogen liquid pump newly and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, or be adjusted into that the first condenser has the cryogen liquid pipeline through newly-increased choke valve and after absorber is communicated with absorber have again the refrigerant vapour passage to be communicated with newly-increased absorber, newly-increased generator also has respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber jointly by absorber and generator.
43. back-heating type the 3rd class absorption heat pump, in the 5th described back-heating type the 3rd class absorption heat pump, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorption-evaporimeter, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the 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, the first evaporimeter or the 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 absorber and absorption-evaporimeter respectively again, newly-increased generator also has the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively, newly-increased generator drives in addition the thermal medium pipeline and is communicated with outside, forms by newly-increased absorption-evaporimeter and newly-increased generator jointly to absorber or common double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber and absorption-evaporimeter.
44. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 7-8 item, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased generator, newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased solution pump, the first evaporimeter had the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively to be adjusted into the 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, the first condenser is set up cryogen liquid pipeline newly-increased absorption-evaporimeter after increasing choke valve newly and newly-increased absorption-evaporimeter is communicated with has the refrigerant vapour passage to be communicated with absorber and absorption-evaporimeter respectively again, or first evaporimeter set up the cryogen liquid pipeline through newly-increased cryogen liquid pump with increase absorption-evaporimeter newly after newly-increased absorption-evaporimeter is communicated with and have again the refrigerant vapour passage to be communicated with absorber and absorption-evaporimeter respectively, newly-increased generator also has the refrigerant vapour passage to be communicated with absorption-evaporimeter and absorber respectively, newly-increased generator drives in addition the thermal medium pipeline and is communicated with outside, forms by newly-increased absorption-evaporimeter and newly-increased generator jointly to absorber or common double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber and absorption-evaporimeter.
45. back-heating type the 3rd class absorption heat pump, in the 41st described back-heating type the 3rd class absorption heat pump, increase newly-increased condenser and newly-increased choke valve, to increase generator newly has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into newly-increased generator to have the refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve, generator and absorber are set up respectively the refrigerant vapour passage and are communicated with the first condenser, newly-increased condenser also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to the first condenser and newly-increased absorber respectively jointly by absorber and generator.
46. back-heating type the 3rd class absorption heat pump, in the 42nd described back-heating type the 3rd class absorption heat pump, increase newly-increased condenser and newly-increased the second choke valve, to increase generator newly has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into newly-increased generator to have the refrigerant vapour passage to be communicated with newly-increased condenser, newly-increased condenser also has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the second choke valve, generator and absorber are set up respectively the refrigerant vapour passage and are communicated with the first condenser, newly-increased condenser also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to the first condenser and newly-increased absorber respectively jointly by absorber and generator.
47. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 11-18 item, increase newly-increased condenser and newly-increased the second choke valve, 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 the first condenser through newly-increased the second choke valve, newly-increased condenser also has the heated medium pipeline to be communicated with outside, forms single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
48. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 19-24 item, increase newly-increased condenser and newly-increased the 3rd choke valve, 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 the first condenser through newly-increased the 3rd choke valve, newly-increased condenser also has the heated medium pipeline to be communicated with outside, forms single-stage triple effect back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
49. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 19-24 item, increase 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 condenser, newly-increased condenser also has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the 3rd choke valve, newly-increased condenser also has the heated medium pipeline to be communicated with outside, forms single-stage triple effect back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
50. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 47-49 item, increase newly-increased first flow control valve and newly-increased second adjustable valve, with the first condenser have the heated medium pipeline with outside is communicated be adjusted into the outside and have the heated medium pipeline to be communicated with the first condenser after the first condenser have again the heated medium pipeline to increase the second adjustable valve newly with outside connected sum warp and be communicated with newly-increased condenser through increasing the first flow choke valve newly respectively, to increase newly condenser have the heated medium pipeline with outside is communicated be adjusted into the first condenser have the heated medium pipeline through newly-increased the second flow throttle valve with increase condenser newly after newly-increased condenser is communicated with and have again the heated medium pipeline to be communicated with the outside, formation adjustable type back-heating type the 3rd class absorption heat pump.
51. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 11-18 item, increase newly-increased the 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 the 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 also has the weak solution pipeline to be communicated with newly-increased the second generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased the second generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased the second generator also has respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order.
52. back-heating type the 3rd class absorption heat pump, in the 51st described back-heating type the 3rd class absorption heat pump, increase newly-increased the second choke valve, to increase newly the second generator have the heated medium pipeline with outside is communicated be adjusted into generator and set up the refrigerant vapour passage and newly-increased the second generator is communicated with after newly-increased the second generator have again the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the second choke valve---the refrigerant vapour conduct of generator release increases the driving thermal medium of the second generator newly, two-stage back-heating type three class absorption heat pump of formation take the single-stage economic benefits and social benefits as the first order.
53. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 11-18 item, increase newly-increased the second generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the second choke valve, newly-increased 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 second generator through newly-increased solution pump and newly-increased solution heat exchanger, newly-increased the second generator also has the concentrated solution pipeline to be communicated with newly-increased absorber through newly-increased solution heat exchanger, newly-increased the second generator also has respectively refrigerant vapour passage and newly-increased condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased condenser also has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the second choke valve, newly-increased absorber and newly-increased condenser also have respectively the heated medium pipeline to be communicated with outside, form two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order.
54. back-heating type the 3rd class absorption heat pump, in the 53rd described back-heating type the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve, to increase newly the second generator have the heated medium pipeline with outside is communicated be adjusted into generator and set up the refrigerant vapour passage and newly-increased the second generator is communicated with after newly-increased the second generator have again the cryogen liquid pipeline to be communicated with newly-increased condenser through newly-increased the 3rd choke valve---the refrigerant vapour conduct of generator release increases the driving thermal medium of the second generator newly, two-stage back-heating type three class absorption heat pump of formation take the single-stage economic benefits and social benefits as the first order.
55. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 19-24 item, increase newly-increased the 3rd generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase the second generator newly has the refrigerant vapour passage to be communicated with the first condenser to be adjusted into newly-increased the 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 respectively refrigerant vapour passage and the first condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber also has the heated medium pipeline to be communicated with outside, forms two-stage back-heating type the 3rd class absorption heat pump take the single-stage triple effect as the first order.
56. back-heating type the 3rd class absorption heat pump, in the 55th described back-heating type the 3rd class absorption heat pump, increase newly-increased the 3rd choke valve, to increase newly the 3rd generator have the heated medium pipeline with outside is communicated be adjusted into generator or newly-increased generator and set up the refrigerant vapour passage and newly-increased the 3rd generator is communicated with after newly-increased the 3rd generator have again the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the 3rd choke valve---the refrigerant vapour conduct of generator or the generation of newly-increased generator increases the driving thermal medium of the 3rd generator, two-stage back-heating type three class absorption heat pump of formation take the single-stage triple effect as the first order newly.
57. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of 19-24 item, 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 3rd choke valve, newly-increased the 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 respectively refrigerant vapour passage and newly-increased condenser connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased condenser also has the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the 3rd choke valve, newly-increased absorber and newly-increased condenser also have respectively the heated medium pipeline to be communicated with outside, form two-stage back-heating type the 3rd class absorption heat pump take the single-stage triple effect as the first order.
58. back-heating type the 3rd class absorption heat pump, in the 57th described back-heating type the 3rd class absorption heat pump, increase newly-increased the 4th choke valve, to increase newly the 3rd generator have the heated medium pipeline with outside is communicated be adjusted into generator or newly-increased generator and set up the refrigerant vapour passage and newly-increased the 3rd generator is communicated with after newly-increased the 3rd generator have again the cryogen liquid pipeline to be communicated with the first condenser through newly-increased the 4th choke valve---the refrigerant vapour conduct of generator or the generation of newly-increased generator increases the driving thermal medium of the 3rd generator, two-stage back-heating type three class absorption heat pump of formation take the single-stage triple effect as the first order newly.
Description of drawings:
Fig. 1 loops back hot type absorption-generation systems the 1st kind of structure and schematic flow sheet according to two-way provided by the present invention.
Fig. 2 loops back hot type absorption-generation systems the 2nd kind of structure and schematic flow sheet according to two-way provided by the present invention.
Fig. 3 loops back hot type absorption-generation systems the 1st kind of structure and schematic flow sheet according to single channel provided by the present invention.
Fig. 4 loops back hot type absorption-generation systems the 2nd kind of structure and schematic flow sheet according to single channel provided by the present invention.
Fig. 5 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 1st kind of structure and schematic flow sheet.
Fig. 6 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 2nd kind of structure and schematic flow sheet.
Fig. 7 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 3rd kind of structure and schematic flow sheet.
Fig. 8 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 4th kind of structure and schematic flow sheet.
Fig. 9 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 5th kind of structure and schematic flow sheet.
Figure 10 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 6th kind of structure and schematic flow sheet.
Figure 11 is according to single-stage single-action back-heating type the 3rd class absorption heat pump provided by the present invention the 7th kind of structure and schematic flow sheet.
Figure 12 is according to provided by the present invention, single-stage parallel double-effect back-heating type the 3rd class absorption heat pump structure and schematic flow sheet.
Figure 13 is according to provided by the present invention, single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 14 is according to provided by the present invention, single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 15 is according to provided by the present invention, single-stage triple effect back-heating type the 3rd class absorption heat pump structure and schematic flow sheet in parallel.
Figure 16 is according to provided by the present invention, single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 17 is according to provided by the present invention, single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 18 is according to provided by the present invention, one generator two-stage back-heating type the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 19 is according to provided by the present invention, one generator two-stage back-heating type the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 20 is according to provided by the present invention, one generator two-stage back-heating type the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet.
Figure 21 is according to provided by the present invention, one generator two-stage back-heating type the 3rd class absorption heat pump the 4th kind of structure and schematic flow sheet.
Figure 22 is according to provided by the present invention, one generator two-stage back-heating type the 3rd class absorption heat pump the 5th kind of structure and schematic flow sheet.
Figure 23 is according to provided by the present invention, one generator two-stage back-heating type the 3rd class absorption heat pump the 6th kind of structure and schematic flow sheet.
Figure 24 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 1st kind of structure and schematic flow sheet.
Figure 25 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 2nd kind of structure and schematic flow sheet.
Figure 26 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 3rd kind of structure and schematic flow sheet.
Figure 27 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 4th kind of structure and schematic flow sheet.
Figure 28 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 5th kind of structure and schematic flow sheet.
Figure 29 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 6th kind of structure and schematic flow sheet.
Figure 30 is according to provided by the present invention, double-generator two-stage back-heating type the 3rd class absorption heat pump the 7th kind of structure and schematic flow sheet.
Figure 31 is according to single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump structure and schematic flow sheet provided by the present invention, take newly-increased condenser as additional high-temperature heat supply end.
Figure 32 is according to adjustable type single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump structure and schematic flow sheet provided by the present invention, take newly-increased condenser as additional high-temperature heat supply end.
Figure 33 is according to provided by the present invention, two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order the 1st kind of structure and schematic flow sheet.
Figure 34 is according to provided by the present invention, two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order the 2nd kind of structure and schematic flow sheet.
Among the figure, 1-absorption-evaporimeter, 2-absorber, 3-the first absorption-generator, 4-the second absorption-generator, 5-generator (rectifying column), 6-the first solution pump, 7-the second solution pump, 8-the 3rd solution pump, 9-solution heat exchanger/the first solution heat exchanger, 10-the second solution heat exchanger, first minute steam chest of 11-, second minute steam chest of 12-, 13-the 4th solution pump, 14-solution choke valve/the first solution choke valve, 15-the second solution choke valve, 16-the first condenser, 17-the second condenser, 18-the first evaporimeter, 19-the second evaporimeter, 20-choke valve/first throttle valve, 21-cryogen liquid pump/the first cryogen liquid pump, 22-the second cryogen liquid pump, 23-the 3rd evaporimeter, 24-the second choke valve, 25-the 3rd choke valve, 26-the 4th choke valve; A-increases generator newly, and B-increases choke valve newly, and C-increases solution heat exchanger newly, D-increases solution pump newly, and E-increases the second generator newly, and F-increases the second choke valve newly, G-increases the second solution heat exchanger newly, and H-increases the second solution pump newly, and I-increases absorption-evaporimeter newly, J-increases the cryogen liquid pump newly, K-increases absorber newly, and L-increases condenser newly, and M-increases the 3rd choke valve newly, N-increases the first flow control valve newly, and O-increases the second adjustable valve newly.
What need to indicate is:
(1) among Fig. 1-4, absorption-evaporimeter 1, the first absorption-generator 1 and second minute steam chest 12 are realized backheat.
(2) Main Function of absorption-evaporimeter 1 is to heat the cryogen liquid of flowing through in it and becomes refrigerant vapour, and the Main Function of the second absorptions-generator 4 is to make the solution of flowing through in it vaporization of being heated, and the two sometimes can be born respectively the part Low Temperature Thermal and load.
When (3) adopting working media take ammonia spirit as representative, this moment, generator was called rectifying column, and the first rectifying column also will increase the heated medium pipeline and be communicated with the outside.
When (4) adopting working media take ammonia spirit as representative, first minute involved steam chest 11 of ammonia spirit increases in case of necessity the cooling medium pipeline and is communicated with the outside.
(5) Figure 1 shows that example, the weak solution of the first absorption-generator 3 is lowered the temperature, flowed through through 10 step-downs of the second solution heat exchanger, and the second absorption-generator 4 absorbs heat and the vaporization of realization part; This moment, the second solution heat exchanger 10 had two effects---and realize the heat exchange between solution and weak solution carried out reducing pressure by regulating flow, weak solution pipeline in 3 outlets of the first absorption-generator increases the solution choke valve in case of necessity, or adopts the solution choke valve to replace the second solution heat exchanger 10---and have a little impact to the heat pump performance index this moment.
Solution circulation was in parallel when (6) " parallel connection " in " single-stage parallel double-effect back-heating type the 3rd class absorption heat pump " referred to back-heating type the 3rd class absorption heat pump realization double-effect process; " single-stage triple effect in parallel " is also like this.
Solution circulation was series connection when (7) " series connection " in " single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump " referred to back-heating type the 3rd class absorption heat pump realization double-effect process; " single-stage serially connected three-effect " is also like this.
(8) be to have quoted the address in the first-class absorption type 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-class absorption type heat pump to call.
(9) among Figure 21, when the pressure reduction between newly-increased absorber K and the first absorption-generator 3 is too small, newly-increased solution heat exchanger C can be set or at the weak solution pipeline that newly-increased absorber K is communicated with the first absorption-generator 3 newly-increased solution pump D be set.
(10) among Figure 18-23, the 26-30, the second absorption-generator 4 externally provides the temperature of thermic load externally to provide the temperature of thermic load to hang down one-level than absorber 2, and the second absorption-generator 4 was born and heated flow through its interior solution and the effect that solution is partly vaporized this moment; When there was suitable thermic load demand the outside, the second absorption-generator 4 is simultaneously externally heat supply still; Similarly situation also has the absorption-evaporimeter 1 among Figure 20-23.
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 in the inessential situation.
Two-way shown in Figure 1 loops back hot type absorption-generation systems and is achieved in that
1. on the structure, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest and second minute steam chest form, absorption-evaporimeter 1 has the weak solution pipeline to be communicated with the first absorption-generator 3 through the 3rd solution pump 8, the first absorption-generator 3 also has the weak solution pipeline to be communicated with first minute steam chest 11 through the second solution heat exchanger 10 and the second absorption-generator 4, steam chest 11 also had the concentrated solution pipeline through the second solution pump 7 in first minute, the second solution heat exchanger 10 and the first absorption-generator 3 are communicated with second minute steam chest 12, steam chest 12 also had the concentrated solution pipeline to be communicated with absorber 2 in second minute, absorber 2 also has the weak solution pipeline to be communicated with absorption-evaporimeter 1, the second absorption-generator 4 has the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9, generator 5 also has the concentrated solution pipeline to be communicated with the second absorption-generator 4 through the first solution heat exchanger 9, absorption-evaporimeter 1 also has the refrigerant vapour passage to be communicated with outside, absorption-evaporimeter 1 had the refrigerant vapour passage to be communicated with the first absorption-generator 3 again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1, absorber 2 also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, steam chest 12 also had the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 in second minute, steam chest 11 also had the refrigerant vapour passage to be communicated with outside in first minute, the second absorption-generator 4 also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, and generator 5 also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside.
2. on the flow process, refrigerant vapour from the outside enters absorber 2, is absorbed also heat release in heated medium by the concentrated solution from second minute steam chest 12, the weak solution of absorber 2 enters absorption-evaporimeter 1, absorb from the refrigerant vapour of second minute steam chest 12 and heat release in the cryogen liquid of the absorption-evaporimeter 1 of flowing through, from the cryogen liquid of outside flow through absorption-evaporimeter 1, absorb heat into refrigerant vapour and provide to the first absorption-generator 3; The weak solution of absorption-evaporimeter 1 enters the first absorption-generator 3 through 8 pressurizations of the 3rd solution pump, absorb the refrigerant vapour of self-absorption-evaporimeter 1 and heat release in the solution of the first absorption-generator 3 of flowing through, the weak solution of the first absorption-generator 3 second absorption-generator 4 of after the second solution heat exchanger 10 decrease temperature and pressure, flowing through again, enter first minute steam chest 11 after the heat absorbing part vaporization, the solution that enters first minute steam chest 11 discharges refrigerant vapour also externally is provided, the concentrated solution of the first minute steam chest 11 first absorption-generator 3 of behind the second solution pump 7 and the second solution heat exchanger 10, flowing through again, enter second minute steam chest 12 after the heat absorbing part vaporization, enter the solution release of second minute steam chest 12 and provide refrigerant vapour to absorption-evaporimeter 1, the concentrated solution of second minute steam chest 12 enters absorber 2; From the refrigerant vapour of outside enter the second absorption-generator 4, absorbed by the concentrated solution from generator 5 and respectively heat release in the solution of heated medium and the second absorption-generator 4 of flowing through, the weak solution of the second absorption-evaporimeter 4 enters generator 5 through the first solution pump 6 and the first solution heat exchanger 9, the solution that the heating of driving thermal medium enters generator 5 externally discharges refrigerant vapour, the concentrated solution of generator 5 enters the second absorption-generator 4 after 9 heat releases of the first solution heat exchanger and step-down, form two-way and loop back hot type absorption-generation systems.
Two-way shown in Figure 2 loops back hot type absorption-generation systems, and with shown in Figure 1 comparing, change shown in Figure 2 has: 1. absorption-evaporimeter 1 increase heated medium pipeline is communicated with outside; 2. increase solution choke valve 14, absorber 2 has the weak solution pipeline to be communicated with absorption-evaporimeter 1 through solution choke valve 14; 3. increasing by 13, the second minutes steam chests 12 of the 4th solution pump is communicated with absorber 2 through the 4th solution pump 13; 4. first minute steam chest 11 increase cooling medium pipeline is communicated with outside; 5. the outside provides refrigerant vapour to absorption-evaporimeter 1, and absorption-evaporimeter 1 also wants heat release in heated medium.
Single channel shown in Figure 3 loops back hot type absorption-generation systems and is achieved in that
1. on the structure, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest and second minute steam chest form, absorption-evaporimeter 1 has the weak solution pipeline to be communicated with the first absorption-generator 3 through the 3rd solution pump 8, the first absorption-generator 3 also has the weak solution pipeline to be communicated with the second absorption-generator 4 through the second solution heat exchanger 10, the second absorption-generator 4 has the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9, generator 5 also has the concentrated solution pipeline to be communicated with first minute steam chest 11 through the first solution heat exchanger 9 and the second absorption-generator 4, steam chest 11 also had the concentrated solution pipeline through the second solution pump 7 in first minute, the second solution heat exchanger 10 and the first absorption-generator 3 are communicated with second minute steam chest 12, steam chest 12 also had the concentrated solution pipeline to be communicated with absorber 2 in second minute, absorber 2 also has the weak solution pipeline to be communicated with absorption-evaporimeter 1, absorption-evaporimeter 1 also has the refrigerant vapour passage to be communicated with outside, absorption-evaporimeter 1 had the refrigerant vapour passage to be communicated with the first absorption-generator 3 again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1, absorber 2 also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, steam chest 12 also had the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 in second minute, steam chest 11 also had the refrigerant vapour passage to be communicated with outside in first minute, the second absorption-generator 4 also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, and generator 5 also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside.
2. on the flow process, refrigerant vapour from the outside enters absorber 2, is absorbed also heat release in heated medium by the concentrated solution from second minute steam chest 12, the weak solution of absorber 2 enters absorption-evaporimeter 1, absorb from the refrigerant vapour of second minute steam chest 12 and heat release in the cryogen liquid of the absorption-evaporimeter 1 of flowing through, from the cryogen liquid of outside flow through absorption-evaporimeter 1, absorb heat into refrigerant vapour and provide to the first absorption-generator 3; The weak solution of absorption-evaporimeter 1 enters the first absorption-generator 3 through 8 pressurizations of the 3rd solution pump, absorb the refrigerant vapour of self-absorption-evaporimeter 1 and heat release in the solution of the first absorption-generator 3 of flowing through, the weak solution of the first absorption-generator 3 enters the second absorption-generator 4 after the second solution heat exchanger 10 decrease temperature and pressure, absorption from the refrigerant vapour of outside and respectively heat release in the solution of heated medium and the second absorption-generator 4 of flowing through, the weak solution of the second absorption-evaporimeter 4 enters generator 5 through the first solution pump 6 and the first solution heat exchanger 9, the solution that the heating of driving thermal medium enters generator 5 externally discharges refrigerant vapour, the concentrated solution of the generator 5 second absorption-generator 4 of after 9 heat releases of the first solution heat exchanger and step-down, flowing through again, enter first minute steam chest 11 after the heat absorbing part vaporization, the solution that enters first minute steam chest 11 discharges refrigerant vapour also externally is provided, the concentrated solution of the first minute steam chest 11 first absorption-generator 3 of behind the second solution pump 7 and the second solution heat exchanger 10, flowing through again, enter second minute steam chest 12 after the heat absorbing part vaporization, enter the solution release of second minute steam chest 12 and provide refrigerant vapour to absorption-evaporimeter 1, the concentrated solution of second minute steam chest 12 enters absorber 2, forms single channel and loops back hot type absorption-generation systems.
Single channel shown in Figure 4 loops back hot type absorption-generation systems, and with shown in Figure 3 comparing, change shown in Figure 4 has: 1. absorption-evaporimeter 1 increase heated medium pipeline is communicated with outside; 2. increase by the first solution choke valve 14, absorber 2 has the weak solution pipeline to be communicated with absorption-evaporimeter 1 through the first solution choke valve 14; 3. increasing by 13, the second minutes steam chests 12 of the 4th solution pump is communicated with absorber 2 through the 4th solution pump 13; 4. cancel the second solution heat exchanger 10, increase by the second solution choke valve 15, steam chest 11 had the concentrated solution pipeline to be communicated with second minute steam chest 12 through the second solution pump 7 and the first absorption-generator 3 in first minute, and the first absorption-generator 3 has the weak solution pipeline to be communicated with the second absorption-generator 4 through the second solution choke valve 15; 5. the outside provides refrigerant vapour to absorption-evaporimeter 1, and absorption-evaporimeter 1 also wants heat release in heated medium.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 5 is achieved in that
1. on the structure, in backheating type absorption-generation systems shown in Figure 1, cancellation the second absorption-generator 4 and the outside heated medium pipeline that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, choke valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator 5 and to have the refrigerant vapour passage to be communicated with the first condenser 16 in generator 5, the first condenser 16 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through choke valve 20, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter 19 and to have the refrigerant vapour passage to be communicated with the second absorption-generator 4 in the second absorption-generator 4, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest 11 and to have the refrigerant vapour passage to be communicated with the second condenser 17 first minute steam chest 11, the second condenser 17 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through the first cryogen liquid pump 21, to absorb-evaporimeter 1 has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorber 2 absorber 2, absorption-evaporimeter 1 has the refrigerant vapour passage to be communicated with the first absorption-generator 3 to be defined as the first evaporimeter 18 to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator 3 through the second cryogen liquid pump 22 with absorption-evaporimeter 1 after absorption-evaporimeter 1 is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1 outside, the first condenser 16 also has the heated medium pipeline to be communicated with outside, the second condenser 17 also has the cooling medium pipeline to be communicated with outside, and the first evaporimeter 18 and the second evaporimeter 19 medium pipeline that also has surplus heat respectively is communicated with the outside.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and becomes cryogen liquid behind heated medium, and the cryogen liquid of the first condenser 16 enters the second evaporimeter 19, absorption waste heat and becomes refrigerant vapour and provide to the second absorption-generator 4 behind choke valve 20 reducing pressure by regulating flows; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release and become cryogen liquid behind cooling medium, the cryogen liquid of the second condenser 17 enters the first evaporimeter 18 after the first cryogen liquid pump 21 boosts, the cryogen liquid that enters the first evaporimeter 18 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to absorber 2, the second the tunnel after the pressurization of the second cryogen liquid pump 22, flow through absorptions-evaporimeter 1, absorb heat into refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump be provided to the first absorption-generator 3.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 6 is achieved in that
1. on the structure, in backheating type absorption-generation systems shown in Figure 2, the heated medium pipeline that cancellation the second absorption-generator 4 externally is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the second choke valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator 5 and to have the refrigerant vapour passage to be communicated with the first condenser 16 in generator 5, the first condenser 16 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through first throttle valve 20, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter 19 and to have the refrigerant vapour passage to be communicated with the second absorption-generator 4 in the second absorption-generator 4, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest 11 and to have the refrigerant vapour passage to be communicated with the second condenser 17 first minute steam chest 11, the second condenser 17 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through the first cryogen liquid pump 21, the first evaporimeter 18 also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter 23 through the second choke valve 24, to absorb-evaporimeter 1 has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter 23 and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorber 2 absorber 2, absorption-evaporimeter 1 has the refrigerant vapour passage to be communicated with the first absorption-generator 3 to be defined as the 3rd evaporimeter 23 to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator 3 through the second cryogen liquid pump 22 with absorption-evaporimeter 1 after absorption-evaporimeter 1 is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1 outside, the first condenser 16 also has the heated medium pipeline to be communicated with outside, the second condenser 17 also has the cooling medium pipeline to be communicated with the first evaporimeter 18 with outside, the second evaporimeter 19 and the 3rd evaporimeter 23 medium pipeline that also has surplus heat respectively is communicated with outside.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and becomes cryogen liquid behind heated medium, and the cryogen liquid of the first condenser 16 enters the second evaporimeter 19, absorption waste heat and becomes refrigerant vapour and provide to the second absorption-generator 4 behind first throttle valve 20 reducing pressure by regulating flows; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release becomes cryogen liquid behind cooling medium, the cryogen liquid of the second condenser 17 enters the first evaporimeter 18 after the first cryogen liquid pump 21 boosts, the cryogen liquid that enters the first evaporimeter 18 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to absorber 2, the second the tunnel enters the 3rd evaporimeter 24 through 24 throttlings of the second choke valve, the cryogen liquid that enters the 3rd evaporimeter 24 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to absorption-evaporimeter 1, the second tunnel absorption-evaporimeter 1 of after the pressurization of the second cryogen liquid pump 22, flowing through, absorb heat into refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump is provided to the first absorption-generator 3.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 7 is achieved in that
1. on the structure, in backheating type absorption-generation systems shown in Figure 3, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the first cryogen liquid pump, the second cryogen liquid pump, first throttle valve and the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator 5 and to have the refrigerant vapour passage to be communicated with the first condenser 16 in generator 5, the first condenser 16 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through first throttle valve 20, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest 11 and to have the refrigerant vapour passage to be communicated with the second condenser 17 first minute steam chest 11, the second condenser 17 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through the first cryogen liquid pump 21, the first evaporimeter 18 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through the second choke valve 24, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter 19 and to have the refrigerant vapour passage to be communicated with the second absorption-generator 4 in the second absorption-generator 4, to absorb-evaporimeter 1 has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorber 2 absorber 2, absorption-evaporimeter 1 has the refrigerant vapour passage to be communicated with the first absorption-generator 3 to be defined as the first evaporimeter 18 to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator 3 through the second cryogen liquid pump 22 with absorption-evaporimeter 1 after absorption-evaporimeter 1 is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1 outside, the first condenser 16 also has the heated medium pipeline to be communicated with outside, the second condenser 17 also has the cooling medium pipeline to be communicated with outside, and the first evaporimeter 18 and the second evaporimeter 19 medium pipeline that also has surplus heat respectively is communicated with the outside.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and become cryogen liquid behind heated medium, and the cryogen liquid of the first condenser 16 enters the first evaporimeter 18 behind first throttle valve 20 reducing pressure by regulating flows; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release and become cryogen liquid behind cooling medium, and the cryogen liquid of the second condenser 17 enters the first evaporimeter 18 after cryogen liquid pump 21 boosts; The cryogen liquid that enters the first evaporimeter 18 is divided into three the tunnel---and first via absorption waste heat becomes refrigerant vapour and provides to absorber 2, the second the tunnel enters the second evaporimeter 19, absorbs waste heat and become refrigerant vapour and provide to the second absorption-generator 4 through 24 throttlings of the second choke valve, Third Road after the pressurization of the second cryogen liquid pump 22, flow through again absorptions-evaporimeter 1, absorb heat into refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump be provided to the first absorption-generator 3.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 8 is achieved in that
1. on the structure, in backheating type absorption-generation systems shown in Figure 3, cancellation the second absorption-generator 4 and the outside heated medium pipeline that is communicated with, absorption-evaporimeter 1 increases the heated medium pipeline and is communicated with outside, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the first throttle valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator 5 and to have the refrigerant vapour passage to be communicated with the first condenser 16 in generator 5, the first condenser 16 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through first throttle valve 20, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest 11 and to have the refrigerant vapour passage to be communicated with the second condenser 17 first minute steam chest 11, the second condenser 17 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through the first cryogen liquid pump 21, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter 19 and to have the refrigerant vapour passage to be communicated with the second absorption-generator 4 in the second absorption-generator 4, to absorb-evaporimeter 1 has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorber 2 absorber 2, absorption-evaporimeter 1 has the refrigerant vapour passage to be communicated with the first absorption-generator 3 to be defined as the first evaporimeter 18 to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator 3 through the second cryogen liquid pump 22 with absorption-evaporimeter 1 after absorption-evaporimeter 1 is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1 outside, the first condenser 16 also has the heated medium pipeline to be communicated with outside, the second condenser 17 also has the cooling medium pipeline to be communicated with outside, and the first evaporimeter 18 and the second evaporimeter 19 medium pipeline that also has surplus heat respectively is communicated with the outside.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and become cryogen liquid behind heated medium, this cryogen liquid enters the first evaporimeter 18 behind first throttle valve 20 reducing pressure by regulating flows, the cryogen liquid that enters the first evaporimeter 18 is divided into three the tunnel---and first via absorption waste heat becomes refrigerant vapour and provides to absorption-evaporimeter 1, the second the tunnel absorbs waste heat becomes refrigerant vapour and provides to absorber 2, Third Road after 22 pressurizations of the second cryogen liquid pump, flow through again absorption-evaporimeter 1, absorb heat into refrigerant vapour and provide to the first absorption-generator 3; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release and become cryogen liquid behind cooling medium, the cryogen liquid of the second condenser 17 enters the second evaporimeter 19 after cryogen liquid pump 21 boosts, the absorption waste heat becomes refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump is provided to the second absorption-generator 4.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 9 is achieved in that
1. on the structure, in backheating type absorption-generation systems shown in Figure 4, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the cryogen liquid pump, the second choke valve, the 3rd choke valve and the 4th choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator 5 and to have the refrigerant vapour passage to be communicated with the first condenser 16 in generator 5, the first condenser 16 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through first throttle valve 20, the second evaporimeter 19 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through the 3rd choke valve 25, the first evaporimeter 18 also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter 23 through the second choke valve 24, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest 11 and to have the refrigerant vapour passage to be communicated with the second condenser 17 first minute steam chest 11, the second condenser 17 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through the first cryogen liquid pump 21, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter 19 and to have the refrigerant vapour passage to be communicated with the second absorption-generator 4 in the second absorption-generator 4, to absorb-evaporimeter 1 has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter 23 and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorber 2 absorber 2, absorption-evaporimeter 1 has the refrigerant vapour passage to be communicated with the first absorption-generator 3 to be defined as the first condenser 16 to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator 3 through the 4th choke valve 26 with absorption-evaporimeter 1 after absorption-evaporimeter 1 is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1 outside, the first condenser 16 also has the heated medium pipeline to be communicated with outside, the second condenser 17 also has the cooling medium pipeline to be communicated with the first evaporimeter 18 with outside, the second evaporimeter 19 and the 3rd evaporimeter 23 medium pipeline that also has surplus heat respectively is communicated with outside.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and become cryogen liquid behind heated medium, this cryogen liquid is divided into two-way---the first via through enter behind first throttle valve 20 reducing pressure by regulating flows the second evaporimeter 19, the second tunnel after 26 throttlings of the 4th choke valve, flow through again absorption-evaporimeter 1, absorb heat into refrigerant vapour and provide to the first absorption-generator 3; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release and become cryogen liquid behind cooling medium, and the cryogen liquid of the second condenser 17 enters the second evaporimeter 19 after cryogen liquid pump 21 boosts; The cryogen liquid that enters the second evaporimeter 19 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to the second absorption-generator 4, and the second the tunnel enters the first evaporimeter 18 through the 3rd choke valve 25; The cryogen liquid that enters the first evaporimeter 18 is divided into two-way---and first via absorption waste heat becomes refrigerant vapour and provides to absorber 2, the second the tunnel after 24 throttlings of the second choke valve, enter the 3rd evaporimeter 23, absorb waste heat and become refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump is provided to absorptions-evaporimeter 1.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 10 is achieved in that
1. on the structure, in back-heating type shown in Figure 9 the 3rd class sorption type heat pump, cancel the second evaporimeter 19 and the 3rd choke valve 25, cancel the cryogen liquid pipeline that the second evaporimeter 19 is communicated with the first evaporimeter 18 through the 3rd choke valve 25, having the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through first throttle valve 20 the first condenser 16 is adjusted into the first condenser 16 and has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through first throttle valve 20, have the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through cryogen liquid pump 21 the second condenser 17 and be adjusted into the second condenser 17 and have the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through cryogen liquid pump 21, the first evaporimeter 18 increases the refrigerant vapour passages and is communicated with the second absorption-generator 4.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and become cryogen liquid behind heated medium, this cryogen liquid is divided into two-way---the first via through enter behind first throttle valve 20 reducing pressure by regulating flows the first evaporimeter 18, the second tunnel after 26 throttlings of the 4th choke valve, flow through again absorption-evaporimeter 1, absorb heat into refrigerant vapour and provide to the first absorption-generator 3; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release and become cryogen liquid behind cooling medium, and the cryogen liquid of the second condenser 17 enters the first evaporimeter 18 after cryogen liquid pump 21 boosts; The cryogen liquid that enters the first evaporimeter 18 is divided into three the tunnel---and first via absorption waste heat becomes refrigerant vapour and provides to the second absorption-generator 4, the the second tunnel absorption waste heat becomes refrigerant vapour and provides to absorber 2, Third Road enters the 3rd evaporimeter 23, absorbs waste heat and become refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump is provided to absorptions-evaporimeter 1 through the second choke valve 24.
Figure 10 is the structural representation of heat pump shown in Figure 9 during without the second evaporimeter 19; When utilizing the latent heat of waste heat medium, what the second evaporimeter 19 was born provides the task of refrigerant vapour then to be born by the first evaporimeter 18 to the second absorption-generator 4---and the first evaporimeter 18 increases the refrigerant vapour passage and is communicated with the second absorption-generator 4.
Single-stage single-action back-heating type the 3rd class absorption heat pump shown in Figure 11 is achieved in that
1. on the structure, in backheating type absorption-generation systems shown in Figure 4, cancellation the second absorption-generator 4 and the outside heated medium pipeline that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the first cryogen liquid pump, the second choke valve and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator 5 and to have the refrigerant vapour passage to be communicated with the first condenser 16 in generator 5, the first condenser 16 also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through first throttle valve 20, the first evaporimeter 18 also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter 23 through the second choke valve 24, there are refrigerant vapour passage and outside the connection to be defined as first minute steam chest 11 and to have the refrigerant vapour passage to be communicated with the second condenser 17 first minute steam chest 11, the second condenser 17 also has the cryogen liquid pipeline to be communicated with the second evaporimeter 19 through the first cryogen liquid pump 21, there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter 19 and to have the refrigerant vapour passage to be communicated with the second absorption-generator 4 in the second absorption-generator 4, to absorb-evaporimeter 1 has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter 23 and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter 1, there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter 18 and to have the refrigerant vapour passage to be communicated with absorber 2 absorber 2, absorption-evaporimeter 1 has the refrigerant vapour passage to be communicated with the first absorption-generator 3 to be defined as the first evaporimeter 18 to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator 3 through the second cryogen liquid pump 22 with absorption-evaporimeter 1 after absorption-evaporimeter 1 is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter 1 outside, the first condenser 16 also has the heated medium pipeline to be communicated with outside, the second condenser 17 also has the cooling medium pipeline to be communicated with the first evaporimeter 18 with outside, the second evaporimeter 19 and the 3rd evaporimeter 23 medium pipeline that also has surplus heat respectively is communicated with outside.
2. on the flow process, the refrigerant vapour that generator 5 produces enters the first condenser 16, heat release and become cryogen liquid behind heated medium, and this cryogen liquid enters the first evaporimeter 18 after 20 throttlings of first throttle valve; The cryogen liquid that enters the first evaporimeter 18 is divided into three the tunnel---and first via absorption waste heat becomes refrigerant vapour and provides to absorber 2, the second the tunnel after 24 throttlings of the second choke valve, enter the 3rd evaporimeter 23, absorb waste heat and become refrigerant vapour and provide to absorptions-evaporimeter 1, Third Road after the second cryogen liquid pump 22 pressurizes absorption-evaporimeter 1, absorb heat into refrigerant vapour and provide to the first absorption-generator 3; The refrigerant vapour of steam chest 11 generations in first minute enters the second condenser 17, heat release and become cryogen liquid behind cooling medium, the cryogen liquid of the second condenser 17 enters the second evaporimeter 19 after the first cryogen liquid pump 21 boosts, the absorption waste heat becomes refrigerant vapour and formation single-stage single-action back-heating type the 3rd class absorption heat pump is provided to the second absorption-generator 4.
Single-stage parallel double-effect back-heating type the 3rd class absorption heat pump shown in Figure 12 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 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 the second absorption-generator 4 through newly-increased solution heat exchanger C, newly-increased generator A has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B again after having the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 to have the refrigerant vapour passage to be communicated with newly-increased generator A the generator 5---and the refrigerant vapour that generator discharges increases generator A newly and also has the refrigerant vapour passage to be communicated with the first condenser 16 as the driving thermal medium that increases generator newly.
2. on the flow process, the part weak solution of the second absorption-generator 4 enters newly-increased generator A through the first solution pump 6 and newly-increased solution heat exchanger C, discharge refrigerant vapour from the refrigerant vapour of generator 5 solution that newly-increased generator A, heating enter newly-increased generator A of flowing through, the refrigerant vapour that newly-increased generator A produces provides to the first condenser 16; The concentrated solution of newly-increased generator A enters the second absorption-generator 4 through newly-increased solution heat exchanger C, the refrigerant vapour heat release that increases generator A newly of flowing through becomes cryogen liquid, enters the first condenser 16 through newly-increased choke valve B throttling again, forms single-stage parallel double-effect back-heating type the 3rd class absorption heat pump.
Single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump shown in Figure 13 is achieved in that
1. on the structure, in back-heating type the 3rd class sorption type heat pump shown in 7, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with first minute steam chest 11 through the first solution heat exchanger 9 and the second absorption-generator 4 in generator 5 is adjusted into generator 5 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 first minute steam chest 11 through the first solution heat exchanger 9 and the second absorption-generator 4, having the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9 in the second absorption-generator 4 is adjusted into the second absorption-generator 4 and the weak solution pipeline is arranged through the first solution pump 6, the first solution heat exchanger 9 and newly-increased solution heat exchanger C are communicated with generator 5, newly-increased generator A has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B again after having the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 to have the refrigerant vapour passage to be communicated with newly-increased generator A the generator 5---and the refrigerant vapour that generator discharges increases generator A newly and also has the refrigerant vapour passage to be communicated with the first condenser 16 as the driving thermal medium that increases generator newly.
2. on the flow process, the weak solution of the second absorption-generator 4 enters generator 5 through the first solution pump 6, the first solution heat exchanger 9 and newly-increased solution heat exchanger C, the refrigerant vapour that generator 5 produces provides to drive thermal medium as it to newly-increased generator A, and the concentrated solution of generator 5 enters newly-increased generator A through newly-increased solution heat exchanger C; The refrigerant vapour heating that increases generator A newly of flowing through enters the weak solution release of newly-increased generator A and provides refrigerant vapour to the first condenser 16, the concentrated solution of newly-increased generator A enters first minute steam chest 11 through the first solution heat exchanger 9 and the second absorption-generator 4, flowing through enters the first condenser 16 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A forms cryogen liquid again, forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
Single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump shown in Figure 12 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, 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 generator 5 through the first solution pump 6 and the first solution heat exchanger 9 in the second absorption-generator 4 is adjusted into the second absorption-generator 4 and has the weak solution pipeline to be communicated with newly-increased generator A through the first solution pump 6 and the first solution heat exchanger 9, newly-increased generator A also has the concentrated solution pipeline to be communicated with generator 5 through newly-increased solution pump D and newly-increased solution heat exchanger C, having the concentrated solution pipeline to be communicated with the second absorption-generator 4 through the first solution heat exchanger 9 in generator 5 is adjusted into generator 5 and has the concentrated solution pipeline to be communicated with the second absorption-generator 4 through newly-increased solution heat exchanger C and the first solution heat exchanger 9, newly-increased generator A has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B again after having the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 to have the refrigerant vapour passage to be communicated with newly-increased generator A the generator 5---and the refrigerant vapour that generator discharges increases generator A newly and also has the refrigerant vapour passage to be communicated with the first condenser 16 as the driving thermal medium that increases generator newly.
2. on the flow process, the refrigerant vapour that generator 5 discharges provides to drive thermal medium as it to newly-increased generator A, the weak solution of the second absorption-generator 4 enters newly-increased generator A through the first solution pump 6 and the first solution heat exchanger 9, the refrigerant vapour heating that increases generator A newly of flowing through enters its interior solution release refrigerant vapour, the refrigerant vapour that newly-increased generator A produces enters the first condenser 16, and the concentrated solution of newly-increased generator A enters generator 5 through newly-increased solution pump D and newly-increased solution heat exchanger C; The concentrated solution of generator 5 enters the second absorption-generator 4 through newly-increased solution heat exchanger C and the first solution heat exchanger 9, flowing through enters the first condenser 16 through newly-increased choke valve B throttling after the refrigerant vapour heat release of newly-increased generator A forms cryogen liquid again, forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
Single-stage shown in Figure 15 triple effect back-heating type in parallel the 3rd class absorption heat pump is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, the first solution pump 6 is set up the weak solution pipeline and is communicated with newly-increased the second generator E through newly-increased the second solution heat exchanger G with newly-increased generator A connected sum through newly-increased solution heat exchanger C respectively, newly-increased generator A also has the concentrated solution pipeline to be communicated with the second absorption-generator 4 through newly-increased solution heat exchanger C, newly-increased the second generator E also has the concentrated solution pipeline to be communicated with the second absorption-generator 4 through newly-increased the second solution heat exchanger G, newly-increased generator A has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B again after having the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 to have the refrigerant vapour passage to be communicated with newly-increased generator A the generator 5---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator E had newly-increased the second choke valve F of cryogen liquid pipeline warp to be communicated with the first condenser 16 again after newly-increased generator A also had refrigerant vapour passage and newly-increased the second generator E to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, and newly-increased the second generator E also has the refrigerant vapour passage to be communicated with the first condenser 16.
2. on the flow process, a part of weak solution of the second absorption-generator 4 enters newly-increased generator A through the first solution pump 6 and newly-increased solution heat exchanger C, the release of generator 5 provides refrigerant vapour to drive thermal medium as it to newly-increased generator A, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to newly-increased the second generator E, and the newly-increased solution heat exchanger C of concentrated solution warp of newly-increased generator A enters the second absorption-generator 4; Another part weak solution of the second absorption-generator 4 enters newly-increased the second generator E through the first solution pump 6 and newly-increased the second solution heat exchanger G, enter solution in it and discharge and provide refrigerant vapour to the first condenser 16 from flow through newly-increased the second generator E, heating of the refrigerant vapour of newly-increased generator A, the concentrated solution of newly-increased the second generator E enters the second absorption-generator 4 through newly-increased the second solution heat exchanger G; The cryogen liquid that the refrigerant vapour heat release of newly-increased generator A of flowing through forms enters the first condenser 16 through newly-increased choke valve B throttling, the cryogen liquid that the refrigerant vapour heat release of newly-increased the second generator E of flowing through forms enters the first condenser 16 through newly-increased the second choke valve F throttling, forms single-stage triple effect back-heating type in parallel the 3rd class absorption heat pump.
Single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump shown in Figure 16 is achieved in that
1. on the structure, in the 3rd class sorption type heat pump shown in Figure 7, cancellation the second absorption-generator 4 and the outside heated medium pipeline that is communicated with, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, having the concentrated solution pipeline to be communicated with first minute steam chest 11 through the first solution heat exchanger 9 and the second absorption-generator 4 in generator 5 is adjusted into generator 5 and has the concentrated solution pipeline to be communicated with newly-increased generator A through the first solution heat exchanger 9, newly-increased generator A also has the newly-increased solution heat exchanger C of concentrated solution pipeline to be communicated with newly-increased the second generator E, newly-increased the second generator E also has the concentrated solution pipeline to be communicated with first minute steam chest 11 through newly-increased the second solution heat exchanger G and the second absorption-generator 4, having the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9 in the second absorption-generator 4 is adjusted into the second absorption-generator 4 and the weak solution pipeline is arranged through the first solution pump 6, newly-increased the second solution heat exchanger G, newly-increased solution heat exchanger C and the first solution heat exchanger 9 are communicated with generator 5, newly-increased generator A has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B again after having the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 to have the refrigerant vapour passage to be communicated with newly-increased generator A the generator 5---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator E had newly-increased the second choke valve F of cryogen liquid pipeline warp to be communicated with the first condenser 16 again after newly-increased generator A also had refrigerant vapour passage and newly-increased the second generator E to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, and newly-increased the second generator E also has the refrigerant vapour passage to be communicated with the first condenser 16.
2. on the flow process, the weak solution of the second absorption-generator 4 is through the first solution pump 6, newly-increased the second solution heat exchanger G, newly-increased solution heat exchanger C and the first solution heat exchanger 9 enter generator 5, the refrigerant vapour that generator 5 produces offers newly-increased generator A to drive thermal medium as it, the concentrated solution of generator 5 enters newly-increased generator A through the first solution heat exchanger 9, refrigerant vapour is flowed through and is increased generator A newly, heating enters its interior solution release and provides refrigerant vapour to newly-increased the second generator E, the concentrated solution of newly-increased generator A enters newly-increased the second generator E through newly-increased solution heat exchanger C, from the refrigerant vapour of newly-increased generator A newly-increased the second generator E that flows through, heating enters its interior solution release and provides refrigerant vapour to the first condenser 16, and the concentrated solution of newly-increased the second generator E enters first minute steam chest 11 through newly-increased the second solution heat exchanger G and the second absorption-generator 4; The cryogen liquid that the refrigerant vapour heat release of newly-increased generator A of flowing through forms enters the first condenser 16 through newly-increased choke valve B throttling, the cryogen liquid that the refrigerant vapour heat release of newly-increased the second generator E of flowing through forms enters the first condenser 16 through newly-increased the second choke valve F throttling, forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
Single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump shown in Figure 17 is achieved in that
1. on the structure, in back-heating type shown in Figure 8 the 3rd class sorption type heat pump, cancellation absorption-evaporimeter 1 and the outside heated medium pipeline that is communicated with, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased solution pump and newly-increased the second solution pump, having the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9 in the second absorption-generator 4 is adjusted into the second absorption-generator 4 and has the weak solution pipeline to be communicated with newly-increased the second generator E through the first solution pump 6 and the first solution heat exchanger 9, newly-increased the second generator E also has the concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased the second solution pump H and newly-increased the second solution heat exchanger G, newly-increased generator A also has the concentrated solution pipeline to be communicated with generator 5 through newly-increased solution pump D and newly-increased solution heat exchanger C, having the concentrated solution pipeline to be communicated with first minute steam chest 11 through the first solution heat exchanger 9 and the second absorption-generator 4 in generator 5 is adjusted into generator 5 and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger C, newly-increased the second solution heat exchanger G, the first solution heat exchanger 9 and the second absorption-generator 4 are communicated with first minute steam chest 11, newly-increased generator A has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B again after having the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 to have the refrigerant vapour passage to be communicated with newly-increased generator A the generator 5---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, newly-increased the second generator E had newly-increased the second choke valve F of cryogen liquid pipeline warp to be communicated with the first condenser 16 again after newly-increased generator A also had refrigerant vapour passage and newly-increased the second generator E to be communicated with---and the refrigerant vapour that newly-increased generator produces is as the driving thermal medium that increases the second generator newly, and newly-increased the second generator E also has the refrigerant vapour passage to be communicated with the first condenser 16.
2. on the flow process, the weak solution of the second absorption-generator 4 enters newly-increased the second generator E through the first solution pump 6 and the first solution heat exchanger 9, the concentrated solution of newly-increased the second generator E enters newly-increased generator A through newly-increased the second solution pump H and newly-increased the second solution heat exchanger G, the concentrated solution of newly-increased generator A enters generator 5 through newly-increased solution pump D and newly-increased solution heat exchanger C, and the concentrated solution of generator 5 enters first minute steam chest 11 through newly-increased solution heat exchanger C, newly-increased the second solution heat exchanger G, the first solution heat exchanger 9 and the second absorption-generator 4; The refrigerant vapour that generator 5 produces offers newly-increased generator A to drive thermal medium as it, the refrigerant vapour heating that increases generator A newly of flowing through enters its interior solution release and provides refrigerant vapour to drive thermal medium as it to newly-increased the second generator E, and the refrigerant vapour heating that increases the second generator E newly of flowing through enters its interior solution release and provides refrigerant vapour to the first condenser 16; The cryogen liquid that the refrigerant vapour heat release of newly-increased generator A of flowing through forms enters the first condenser 16 through newly-increased choke valve B throttling, the cryogen liquid that the refrigerant vapour heat release of newly-increased the second generator E of flowing through forms enters the first condenser 16 through newly-increased the second choke valve F throttling, forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
One generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 180 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, to absorb-evaporimeter 1 has the weak solution pipeline to be communicated with the first absorption-generator 3 through the 3rd solution pump 8 to be adjusted into absorption-evaporimeter 1 and to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter I through newly-increased solution heat exchanger C, newly-increased absorption-evaporimeter I has the weak solution pipeline to be communicated with the first absorption-generator 3 through the 3rd solution pump 8 and newly-increased solution heat exchanger C again, the first evaporimeter 18 had the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively to be adjusted into the first evaporimeter 8 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter I, the first evaporimeter 18 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump J with increase absorption-evaporimeter I newly after newly-increased absorption-evaporimeter I is communicated with and have again the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively.
2. on the flow process, the weak solution of absorption-evaporimeter 1 enters newly-increased absorption-evaporimeter I, absorbs from refrigerant vapour and the heat release of the first evaporimeter 18 and the cryogen liquid of the newly-increased absorption-evaporimeter I that flows through through newly-increased solution heat exchanger C, and the weak solution of newly-increased absorption-evaporimeter I enters the first absorption-generator 3 through the 3rd solution pump 8 and newly-increased solution heat exchanger C; One road cryogen liquid of the first evaporimeter 18 after newly-increased cryogen liquid pump J pressurization, flow through again newly-increased absorptions-evaporimeter I, absorb heat into refrigerant vapour and provide to absorber 2, form by increasing absorption-evaporimeter newly one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour be provided to absorber.
One generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 19 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, there is the weak solution pipeline to be communicated with absorption-evaporimeter 1 to be adjusted into absorber 2 to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter I through newly-increased solution heat exchanger C absorber 2, newly-increased absorption-evaporimeter I has the weak solution pipeline to be communicated with absorption-evaporimeter 1 through newly-increased solution pump D and newly-increased solution heat exchanger C again, the first evaporimeter 18 had the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively to be adjusted into the first evaporimeter 8 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter I, the first evaporimeter 18 set up the cryogen liquid pipeline through newly-increased cryogen liquid pump J with increase absorption-evaporimeter I newly after newly-increased absorption-evaporimeter I is communicated with and have again the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively.
2. on the flow process, refrigerant vapour and heat release that the weak solution of absorber 2 enters through newly-increased solution heat exchanger C and increases absorption-evaporimeter I newly, absorbs from the first evaporimeter 18 increase the cryogen liquid of absorption-evaporimeter I newly in flowing through, the weak solution of newly-increased absorption-evaporimeter I enters absorption-evaporimeter 1 through increasing solution pump D and newly-increased solution heat exchanger C newly; One road cryogen liquid of the first evaporimeter 18 after newly-increased cryogen liquid pump J pressurization, flow through again newly-increased absorptions-evaporimeter I, absorb heat into refrigerant vapour and provide to absorber 2, form by increasing absorption-evaporimeter newly one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour be provided to absorber.
One generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 20 is achieved in that
1. on the structure, in back-heating type shown in Figure 7 the 3rd class sorption type heat pump, cancellation the second absorption-generator 4 and the outside heated medium pipeline that is communicated with, increase newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased solution pump, second minute steam chest 12 had the concentrated solution pipeline to be communicated with absorber 2 to be adjusted into second minute steam chest 12 has the concentrated solution pipeline to be communicated with absorber 2 through newly-increased solution pump D and newly-increased solution heat exchanger C, there is the weak solution pipeline to be communicated with absorption-evaporimeter 1 to be adjusted into absorber 2 to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter I through newly-increased solution heat exchanger C absorber 2, newly-increased absorption-evaporimeter I also has the weak solution pipeline to be communicated with absorption-evaporimeter 1, the first evaporimeter 18 had the refrigerant vapour passage to be communicated with absorber 2 to be adjusted into the first evaporimeter 18 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter I, the first condenser 16 set up the cryogen liquid pipeline through newly-increased choke valve B with increase absorption-evaporimeter I newly after newly-increased absorption-evaporimeter I is communicated with and have again the refrigerant vapour passage to be communicated with absorber 2.
2. on the flow process, the refrigerant vapour of the first evaporimeter 18 provides to newly-increased absorption-evaporimeter I, one road cryogen liquid of the first condenser 16 after newly-increased choke valve B throttling, flow through again newly-increased absorption-evaporimeter I, absorb heat into refrigerant vapour and provide to absorber 2; The concentrated solution of second minute steam chest 12 enters absorber 2 through newly-increased solution pump D and newly-increased solution heat exchanger C, absorption from the refrigerant vapour of newly-increased absorption-evaporimeter I and heat release in heated medium, the weak solution of absorber 2 enters newly-increased absorption-evaporimeter I through newly-increased solution heat exchanger C, absorption increases the cryogen liquid of absorption-evaporimeter I newly from refrigerant vapour and the heat release of the first evaporimeter 18 in flowing through, the weak solution of newly-increased absorption-evaporimeter I enters absorption-evaporimeter 1, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
One generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 21 is achieved in that
1. on the structure, in back-heating type shown in Figure 8 the 3rd class absorption heat pump, cancellation absorption-evaporimeter 1 and the outside heated medium pipeline that is communicated with, increase newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, to absorb-evaporimeter 1 has the weak solution pipeline to be communicated with the first absorption-generator 3 through the 3rd solution pump 8 to be adjusted into absorption-evaporimeter 1 and to have the weak solution pipeline to be communicated with newly-increased absorber K through the 3rd solution pump 8 and newly-increased solution heat exchanger C, newly-increased absorber K also has the weak solution pipeline to be communicated with the first absorption-generator 3 through newly-increased solution heat exchanger C, with absorber 2 have the heated medium pipeline with outside is communicated be adjusted into the first condenser 16 set up the cryogen liquid pipeline through newly-increased choke valve B with increase absorber 2 newly after absorber 2 is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber K, increase absorber K newly and also have the heated medium pipeline to be communicated with the outside.
2. on the flow process, one road cryogen liquid of the first condenser 16 after newly-increased choke valve B throttling, flow through absorber 2, absorb heat into refrigerant vapour and provide to newly-increased absorber K, the weak solution of absorption-evaporimeter 1 enters newly-increased absorber K, absorbs from the refrigerant vapour of absorber 2 and heat release in heated medium through the 3rd solution pump 8 and newly-increased solution heat exchanger C, the weak solution of newly-increased absorber K enters the first absorption-generator 3 through newly-increased solution heat exchanger C, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
One generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 22 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with the second absorption-generator 4 through the first solution heat exchanger 9 in generator 5 is adjusted into generator 5 and has the concentrated solution pipeline to be communicated with newly-increased absorber K through the first solution heat exchanger 9, newly-increased absorber K also has the weak solution pipeline to be communicated with the second absorption-generator 4 through newly-increased solution heat exchanger C, having the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9 in the second absorption-generator 4 is adjusted into the second absorption-generator 4 and the weak solution pipeline is arranged through the first solution pump 6, newly-increased solution heat exchanger C and the first solution heat exchanger 9 are communicated with generator 5, with absorber 2 have the heated medium pipeline with outside is communicated be adjusted into that the second evaporimeter 19 is set up the cryogen liquid pipeline through newly-increased cryogen liquid pump J and after absorber 2 is communicated with absorber 2 have again the refrigerant vapour passage to be communicated with newly-increased absorber K, increase absorber K newly and also have the heated medium pipeline to be communicated with the outside.
2. on the flow process, one road cryogen liquid of the second evaporimeter 19 is through increasing the absorber 2 of flowing through again after cryogen liquid pump J pressurizes newly, absorb heat into refrigerant vapour and provide to newly-increased absorber K, the weak solution of the second absorption-generator 4 is through the first solution pump 6, newly-increased solution heat exchanger C and the first solution heat exchanger 9 enter generator 5, the concentrated solution of generator 5 enters newly-increased absorber K through the first solution heat exchanger 9, absorption from the refrigerant vapour of absorber 2 and heat release in heated medium, the weak solution of newly-increased absorber K enters the second absorption-generator 4 through newly-increased solution heat exchanger C, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
One generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 23 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, 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 the second absorption-generator 4 through the first solution heat exchanger 9 in generator 5 is adjusted into generator 5 and has the concentrated solution pipeline to be communicated with the second absorption-generator 4 through the first solution heat exchanger 9 and newly-increased solution heat exchanger C, having the weak solution pipeline to be communicated with generator 5 through the first solution pump 6 and the first solution heat exchanger 9 in the second absorption-generator 4 is adjusted into the second absorption-generator 4 and has the weak solution pipeline to be communicated with newly-increased absorber K through the first solution pump 6 and newly-increased solution heat exchanger C, newly-increased absorber K also has the weak solution pipeline to be communicated with generator 5 through newly-increased solution pump D and the first solution heat exchanger 9, with absorber 2 have the heated medium pipeline with outside is communicated be adjusted into that the second evaporimeter 19 is set up the cryogen liquid pipeline through newly-increased cryogen liquid pump J and after absorber 2 is communicated with absorber 2 have again the refrigerant vapour passage to be communicated with newly-increased absorber K, increase absorber K newly and also have the heated medium pipeline to be communicated with the outside.
2. on the flow process, the cryogen liquid of the second evaporimeter 19 is through increasing the absorber 2 of flowing through again after cryogen liquid pump J pressurizes newly, absorb heat into refrigerant vapour and provide to newly-increased absorber K, the weak solution of the second absorption-generator 4 enters newly-increased absorber K through the first solution pump 6 and newly-increased solution heat exchanger C, absorption from the refrigerant vapour of absorber 2 and heat release in heated medium, the weak solution of newly-increased absorber K enters generator 5 through newly-increased solution pump D and the first solution heat exchanger 9, the concentrated solution of generator 5 enters the second absorption-generator 4 through the first solution heat exchanger 9 and newly-increased solution heat exchanger C, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 24 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator 5 had the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 has the refrigerant vapour passage to be communicated with newly-increased absorber K, newly-increased absorber K also has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber K through newly-increased solution heat exchanger C, newly-increased generator A also has respectively refrigerant vapour passage and the first condenser 16 connected sums to have the thermal medium of driving pipeline to be communicated with outside, and newly-increased absorber K also has the heated medium pipeline to be communicated with outside.
2. on the flow process, the refrigerant vapour that generator 5 discharges enters newly-increased absorber K, absorbed also heat release in heated medium by the concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber K enters newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, driving the thermal medium heating enters the solution release of newly-increased generator A and provides refrigerant vapour to the first condenser 16, the concentrated solution of newly-increased generator A enters newly-increased absorber K through newly-increased solution heat exchanger C, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by generator.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 25 is achieved in that
1. on the structure, in back-heating type shown in Figure 8 the 3rd class sorption type heat pump, cancellation absorption-evaporimeter 1 and the outside heated medium pipeline that is communicated with, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorber, newly-increased condenser and newly-increased choke valve, generator 5 is set up the refrigerant vapour passage and is communicated with newly-increased absorber K, newly-increased absorber K also has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber K through newly-increased solution heat exchanger C, newly-increased generator A also has the refrigerant vapour passage to be communicated with newly-increased condenser L, newly-increased condenser L also has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased choke valve B, newly-increased generator A drives in addition the thermal medium pipeline and is communicated with outside, and newly-increased absorber K and newly-increased condenser L also have respectively the heated medium pipeline to be communicated with outside.
2. on the flow process, a part of refrigerant vapour of generator 5 enters newly-increased absorber K, absorbed also heat release in heated medium by the concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber K enters newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, driving the thermal medium heating enters the solution release of newly-increased generator A and provides refrigerant vapour to newly-increased condenser L, the refrigerant vapour heat release that enters newly-increased condenser L becomes cryogen liquid in heated medium, newly-increased condenser L cryogen liquid enters the first condenser 16 after newly-increased choke valve B throttling, the concentrated solution of newly-increased generator A enters newly-increased absorber K through newly-increased solution heat exchanger C, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to the first condenser and newly-increased absorber respectively by generator.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 26 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, the first evaporimeter 18 had the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively to be adjusted into the first evaporimeter 18 has the refrigerant vapour passage to be communicated with newly-increased absorber K, newly-increased absorber K also has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber K through newly-increased solution heat exchanger C, newly-increased generator A also has the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively, newly-increased generator A drives in addition the thermal medium pipeline and is communicated with outside, and newly-increased absorber K also has the heated medium pipeline to be communicated with outside.
2. on the flow process, the refrigerant vapour of the first evaporimeter 18 enters newly-increased absorber K, absorbed also heat release in heated medium by the concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber K enters newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, driving the thermal medium heating enters the solution release of newly-increased generator A and provides refrigerant vapour to absorber 2, the concentrated solution of newly-increased generator A enters newly-increased absorber K through newly-increased solution heat exchanger C, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased generator.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 27 is to realize like this;
In back-heating type shown in Figure 26 the 3rd class absorption heat pump, 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 L, newly-increased condenser L also has the cryogen liquid pipeline to be communicated with the first evaporimeter 18 through newly-increased choke valve B, newly-increased condenser L also has the heated medium pipeline to be communicated with outside, forms by newly-increased generator and provides double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour to increasing condenser and absorber newly respectively.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 28 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator 5 had the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into generator 5 has the refrigerant vapour passage to be communicated with newly-increased absorber K, newly-increased absorber K also has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased generator A also has the concentrated solution pipeline to be communicated with newly-increased absorber K through newly-increased solution heat exchanger C, with absorber 2 have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter 19 set up the cryogen liquid pipeline through increase cryogen liquid pump J newly and after absorber 2 is communicated with absorber 2 have again the refrigerant vapour passage to be communicated with newly-increased absorber K, newly-increased generator A also has respectively refrigerant vapour passage and the first condenser 16 connected sums to have the thermal medium of driving pipeline to be communicated with outside, and newly-increased absorber K also has the heated medium pipeline to be communicated with outside.
2. on the flow process, the cryogen liquid of the second evaporimeter 19 after newly-increased cryogen liquid pump J pressurization, flow through absorber 2, absorb heat into refrigerant vapour and provide to newly-increased absorber K, the refrigerant vapour of generator 5 releases provides to newly-increased absorber K; The refrigerant vapour that enters newly-increased absorber K is absorbed also heat release in heated medium by the concentrated solution from newly-increased generator A, the weak solution of newly-increased absorber K enters newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, driving the thermal medium heating enters the solution release of newly-increased generator A and provides refrigerant vapour to the first condenser 16, the concentrated solution of newly-increased generator A enters newly-increased absorber K through newly-increased solution heat exchanger C, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber jointly by absorber and generator.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 29 is achieved in that
1. on the structure, in back-heating type shown in Figure 5 the 3rd class sorption type heat pump, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorption-evaporimeter, the first evaporimeter 18 had the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively to be adjusted into the first evaporimeter 18 has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter I, newly-increased absorption-evaporimeter I also has the weak solution pipeline to be communicated with newly-increased generator A through newly-increased solution pump D 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 I through newly-increased solution heat exchanger C, the first evaporimeter 18 is set up cryogen liquid pipeline newly-increased absorption-evaporimeter I after increasing cryogen liquid pump J newly and newly-increased absorption-evaporimeter I is communicated with has the refrigerant vapour passage to be communicated with absorber 2 and absorption-evaporimeter 1 respectively again, and newly-increased generator A also has the refrigerant vapour passage to be communicated with absorption-evaporimeter 1 and absorber 2 respectively.
2. on the flow process, the refrigerant vapour that the first evaporimeter 18 produces enters newly-increased absorption-evaporimeter I, is absorbed also heat release in the cryogen liquid of the newly-increased absorption-evaporimeter I that flows through by the concentrated solution from newly-increased generator A, the weak solution of newly-increased absorption-evaporimeter I enters newly-increased generator A through newly-increased solution pump D and newly-increased solution heat exchanger C, drive the thermal medium heating and enter the solution release of newly-increased generator A and provide refrigerant vapour to absorber 2, the concentrated solution of newly-increased generator A enters newly-increased absorption-evaporimeter I through newly-increased solution heat exchanger C; One road cryogen liquid of the first evaporimeter 18 after newly-increased cryogen liquid pump J pressurization, flow through newly-increased absorptions-evaporimeter I, absorb heat into refrigerant vapour and provide to absorber 2, form by increasing absorption-evaporimeter and newly-increased generator newly double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour be provided to absorber jointly.
Double-generator two-stage back-heating type the 3rd class absorption heat pump shown in Figure 30 is achieved in that
In back-heating type shown in Figure 28 the 3rd class absorption heat pump, increase newly-increased condenser and newly-increased the second choke valve, to increase generator A newly has the refrigerant vapour passage to be communicated with the first condenser 16 to be adjusted into newly-increased generator A to have the refrigerant vapour passage to be communicated with newly-increased condenser L, newly-increased condenser L also has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased the second choke valve F, generator 5 and absorber 2 are set up respectively the refrigerant vapour passage and are communicated with the first condenser 16, newly-increased condenser L also has the heated medium pipeline to be communicated with outside, and formation is provided respectively double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour jointly to the first condenser and newly-increased absorber by absorber and generator.
Single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end shown in Figure 31 is achieved in that
In single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump shown in Figure 12, increase newly-increased condenser and newly-increased the second choke valve, generator 5 is set up the refrigerant vapour passage and is communicated with newly-increased condenser L, newly-increased condenser L also has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased the second choke valve F, newly-increased condenser L also has the heated medium pipeline to be communicated with outside, forms single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
Adjustable type single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end shown in Figure 32 is achieved in that
In back-heating type shown in Figure 31 the 3rd class absorption heat pump, increase newly-increased first flow control valve and newly-increased second adjustable valve, with the first condenser 16 have the heated medium pipeline with outside is communicated be adjusted into the outside and have the heated medium pipeline to be communicated with the first condenser 16 after the first condenser 16 have again the heated medium pipeline to increase second adjustable valve O newly with outside connected sum warp and be communicated with newly-increased condenser L through increasing first flow choke valve N newly respectively, to increase newly condenser L have the heated medium pipeline with outside is communicated be adjusted into the first condenser 16 have the heated medium pipeline through newly-increased the second flow throttle valve O with increase condenser L newly after newly-increased condenser L is communicated with and have again the heated medium pipeline to be communicated with the outside, formation adjustable type back-heating type the 3rd class absorption heat pump.
Two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order shown in Figure 33 is achieved in that
1. on the structure, in single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump shown in Figure 12, increase newly-increased the 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 the first condenser 16 to be adjusted into newly-increased generator A to have the refrigerant vapour passage to be communicated with newly-increased absorber K, newly-increased absorber K also has the weak solution pipeline to be communicated with newly-increased the second generator E through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased the second generator E also has the concentrated solution pipeline to be communicated with newly-increased absorber K through newly-increased solution heat exchanger C, newly-increased the second generator E also has respectively refrigerant vapour passage and the first condenser 16 connected sums to have the thermal medium of driving pipeline to be communicated with outside, and newly-increased absorber K also has the heated medium pipeline to be communicated with outside.
2. on the flow process, the second level flow process of lifting waste heat supply temperature is performed such: a part of refrigerant vapour that newly-increased generator A produces enters newly-increased absorber K, absorbed also heat release in heated medium by the concentrated solution from newly-increased the second generator E, the weak solution of newly-increased absorber K enters newly-increased the second generator E through newly-increased solution pump D and newly-increased solution heat exchanger C, driving the thermal medium heating enters the solution release of newly-increased the second generator E and provides refrigerant vapour to the first condenser 16, the concentrated solution of newly-increased the second generator E enters newly-increased absorber K through newly-increased solution heat exchanger C, forms two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order.
Two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order shown in Figure 34 is achieved in that
1. on the structure, in single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump shown in Figure 12, increase newly-increased the second generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser, newly-increased the second choke valve and newly-increased the 3rd choke valve, newly-increased generator A sets up the refrigerant vapour passage and is communicated with newly-increased absorber K, newly-increased absorber K also has the weak solution pipeline to be communicated with newly-increased the second generator E through newly-increased solution pump D and newly-increased solution heat exchanger C, newly-increased the second generator E also has the concentrated solution pipeline to be communicated with newly-increased absorber K through newly-increased solution heat exchanger C, newly-increased the second generator E also has the refrigerant vapour passage to be communicated with newly-increased condenser L, newly-increased the second generator E had the cryogen liquid pipeline to be communicated with newly-increased condenser L through newly-increased the 3rd choke valve M again after generator 5 was set up refrigerant vapour passage and newly-increased the second generator E and is communicated with---and a part of refrigerant vapour conduct of generator 5 generations increases the driving thermal medium of the second generator E newly, newly-increased condenser L also has the cryogen liquid pipeline to be communicated with the first condenser 16 through newly-increased the second choke valve F, and newly-increased absorber K and newly-increased condenser L also have respectively the heated medium pipeline to be communicated with outside.
2. on the flow process, the second level flow process of lifting waste heat supply temperature is performed such: a part of refrigerant vapour that newly-increased generator A produces enters newly-increased absorber K, absorbed also heat release in heated medium by the concentrated solution from newly-increased the second generator E, the weak solution of newly-increased absorber K enters newly-increased the second generator E through newly-increased solution pump D and newly-increased solution heat exchanger C, from the refrigerant vapour of generator 5 newly-increased the second generator E that flows through, heating enters the solution release of newly-increased the second generator E and provides refrigerant vapour to newly-increased condenser L, the concentrated solution of newly-increased the second generator E enters newly-increased absorber K through newly-increased solution heat exchanger C, and the refrigerant vapour heat release of newly-increased the second generator E that flows through enters newly-increased condenser L through newly-increased the 3rd choke valve M throttling after becoming cryogen liquid again; The refrigerant vapour heat release that enters newly-increased condenser L becomes cryogen liquid in heated medium, and the cryogen liquid of newly-increased condenser L enters the first condenser 16 through newly-increased the second choke valve F throttling, forms two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order.
The effect that the technology of the present invention can realize---backheating type absorption-generation systems and back-heating type 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 back-heating type 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 back-heating type the 3rd class absorption heat pump that proposes has enriched absorption heat pump, can realize better the mutual coupling between heat pump heat supply and user's heat.
4. utilize serial back-heating type the 3rd class absorption heat pump provided by the invention, can make and realize continuously correspondingly between the running parameter of single source pump and the performance index, can realize the continuous linking on running parameter and performance index between the adjacent heat pump assembly.
5. serial back-heating type 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 source pump and keeps the superior performance index, improves efficiency of energy utilization.

Claims (58)

1. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest and second minute steam chest form, absorption-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8), the first absorption-generator (3) also have the weak solution pipeline through the second solution heat exchanger (10) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, first minute steam chest (11) also have the concentrated solution pipeline through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with, second minute steam chest (12) also have the concentrated solution pipeline to be communicated with absorber (2), absorber (2) also has the weak solution pipeline to be communicated with absorption-evaporimeter (1), the second absorption-generator (4) has the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9), generator (5) also has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9), absorption-evaporimeter (1) also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter (1) had the refrigerant vapour passage to be communicated with the first absorption-generator (3) again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1), absorber (2) also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, second minute steam chest (12) also have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), first minute steam chest (11) also have the refrigerant vapour passage to be communicated with or also to have respectively refrigerant vapour passage and outside connected sum to have the cooling medium pipeline to be communicated with the outside with outside, the second absorption-generator (4) also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator (5) also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms two-way and loops back hot type absorption-generation systems; Wherein, or adopt solution choke valve (14) to replace the second solution heat exchanger (10), with the first absorption-generator (3) have the weak solution pipeline through the second solution heat exchanger (10) and the second absorption-generator (4) with first minute steam chest (11) be communicated with change to the first absorption-generator (3) have the weak solution pipeline through solution choke valve (14) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, with first minute steam chest (11) the concentrated solution pipeline is arranged through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with change to first minute steam chest (11) have the concentrated solution pipeline through the second solution pump (7) and the first absorption-generator (3) with second minute steam chest (12) be communicated with.
2. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest, second minute steam chest, the 4th solution pump and solution choke valve form, absorption-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8), the first absorption-generator (3) also have the weak solution pipeline through the second solution heat exchanger (10) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, first minute steam chest (11) also have the concentrated solution pipeline through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with, second minute steam chest (12) also have the concentrated solution pipeline to be communicated with absorber (2) through the 4th solution pump (13), absorber (2) also has the weak solution pipeline to be communicated with absorption-evaporimeter (1) through solution choke valve (14), the second absorption-generator (4) has the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9), generator (5) also has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9), absorption-evaporimeter (1) also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter (1) had the refrigerant vapour passage to be communicated with the first absorption-generator (3) again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1), absorber (2) also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, second minute steam chest (12) also have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), first minute steam chest (11) also have the refrigerant vapour passage to be communicated with or also to have respectively refrigerant vapour passage and outside connected sum to have the cooling medium pipeline to be communicated with the outside with outside, the second absorption-generator (4) also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator (5) also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms two-way and loops back hot type absorption-generation systems; Wherein, or adopt the second solution choke valve (15) to replace the second solution heat exchanger (10), with the first absorption-generator (3) have the weak solution pipeline through the second solution heat exchanger (10) and the second absorption-generator (4) with first minute steam chest (11) be communicated with change to the first absorption-generator (3) have the weak solution pipeline through the second solution choke valve (15) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, with first minute steam chest (11) the concentrated solution pipeline is arranged through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with change to first minute steam chest (11) have the concentrated solution pipeline through the second solution pump (7) and the first absorption-generator (3) with second minute steam chest (12) be communicated with.
3. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest and second minute steam chest form, absorption-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8), the first absorption-generator (3) also has the weak solution pipeline to be communicated with the second absorption-generator (4) through the second solution heat exchanger (10), the second absorption-generator (4) also has the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9), generator (5) also have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, first minute steam chest (11) also have the concentrated solution pipeline through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with, second minute steam chest (12) also have the concentrated solution pipeline to be communicated with absorber (2), absorber (2) also has the weak solution pipeline to be communicated with absorption-evaporimeter (1), absorption-evaporimeter (1) also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter (1) had the refrigerant vapour passage to be communicated with the first absorption-generator (3) again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1), absorber (2) also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, second minute steam chest (12) also have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), first minute steam chest (11) also have the refrigerant vapour passage to be communicated with the outside, the second absorption-generator (4) also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator (5) also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms single channel and loops back hot type absorption-generation systems; Wherein, or adopt solution choke valve (14) to replace the second solution heat exchanger (10), have the weak solution pipeline to be communicated with the second absorption-generator (4) through the second solution heat exchanger (10) in the first absorption-generator (3) and change to the first absorption-generator (3) and have the weak solution pipeline to be communicated with the second absorption-generator (4) through solution choke valve (14), with first minute steam chest (11) the concentrated solution pipeline is arranged through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with change to first minute steam chest (11) have the concentrated solution pipeline through the second solution pump (7) and the first absorption-generator (3) with second minute steam chest (12) be communicated with.
4. backheating type absorption-generation systems, it is mainly by absorption-evaporimeter, absorber, the first absorption-generator, the second absorption-generator, generator, the first solution pump, the second solution pump, the 3rd solution pump, the first solution heat exchanger, the second solution heat exchanger, first minute steam chest, second minute steam chest, the 4th solution pump and solution choke valve form, absorption-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8), the first absorption-generator (3) also has the weak solution pipeline to be communicated with the second absorption-generator (4) through the second solution heat exchanger (10), the second absorption-generator (4) also has the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9), generator (5) also have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, first minute steam chest (11) also have the concentrated solution pipeline through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with, second minute steam chest (12) also have the concentrated solution pipeline to be communicated with absorber (2) through the 4th solution pump (13), absorber (2) also has the weak solution pipeline to be communicated with absorption-evaporimeter (1) through solution choke valve (14), absorption-evaporimeter (1) also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, absorption-evaporimeter (1) had the refrigerant vapour passage to be communicated with the first absorption-generator (3) again after the outside had the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1), absorber (2) also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, second minute steam chest (12) also have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), first minute steam chest (11) also have the refrigerant vapour passage to be communicated with the outside, the second absorption-generator (4) also has the refrigerant vapour passage to be communicated with the outside or also has respectively refrigerant vapour passage and outside connected sum to have the heated medium pipeline to be communicated with outside, generator (5) also has respectively refrigerant vapour passage and outside connected sum to have the thermal medium of driving pipeline to be communicated with outside, forms single channel and loops back hot type absorption-generation systems; Wherein, or adopt the second solution choke valve (15) to replace the second solution heat exchanger (10), have the weak solution pipeline to be communicated with the second absorption-generator (4) through the second solution heat exchanger (10) in the first absorption-generator (3) and change to the first absorption-generator (3) and have the weak solution pipeline to be communicated with the second absorption-generator (4) through the second solution choke valve (15), with first minute steam chest (11) the concentrated solution pipeline is arranged through the second solution pump (7), the second solution heat exchanger (10) and the first absorption-generator (3) with second minute steam chest (12) be communicated with change to first minute steam chest (11) have the concentrated solution pipeline through the second solution pump (7) and the first absorption-generator (3) with second minute steam chest (12) be communicated with.
5. back-heating type the 3rd class absorption heat pump, in backheating type absorption-generation systems claimed in claim 1, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, choke valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator (5) and to have the refrigerant vapour passage to be communicated with the first condenser (16) in generator (5), the first condenser (16) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through choke valve (20), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (19) and to have the refrigerant vapour passage to be communicated with the second absorption-generator (4) in the second absorption-generator (4), with first minute steam chest (11) have the refrigerant vapour passage with outside be communicated be defined as first minute steam chest (11) have the refrigerant vapour passage to be communicated with the second condenser (17), the second condenser (17) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21), to absorb-evaporimeter (1) has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorber (2) absorber (2), absorption-evaporimeter (1) has the refrigerant vapour passage to be communicated with the first absorption-generator (3) to be defined as the first evaporimeter (18) or the second condenser (17) to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second cryogen liquid pump (22) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1) outside, the first condenser (16) also has the heated medium pipeline to be communicated with outside, the second condenser (17) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (18) and the second evaporimeter (19) medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein, during without the second evaporimeter (19), the first condenser (16) has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through choke valve (20) to change to the first condenser (16) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through choke valve (20), and the first evaporimeter (18) increases the refrigerant vapour passage and is communicated with the second absorption-generator (4).
6. back-heating type the 3rd class absorption heat pump, in backheating type absorption-generation systems claimed in claim 2, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the second choke valve, the first cryogen liquid pump and the second cryogen liquid pump, there are refrigerant vapour passage and outside the connection to be defined as generator (5) and to have the refrigerant vapour passage to be communicated with the first condenser (16) in generator (5), the first condenser (16) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through first throttle valve (20), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (19) and to have the refrigerant vapour passage to be communicated with the second absorption-generator (4) in the second absorption-generator (4), with first minute steam chest (11) have the refrigerant vapour passage with outside be communicated be defined as first minute steam chest (11) have the refrigerant vapour passage to be communicated with the second condenser (17), the second condenser (17) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21), the first evaporimeter (18) also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter (23) through the second choke valve (24), to absorb-evaporimeter (1) has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter (23) and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorber (2) absorber (2), absorption-evaporimeter (1) has the refrigerant vapour passage to be communicated with the first absorption-generator (3) to be defined as the 3rd evaporimeter (23) or the first evaporimeter (18) to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second cryogen liquid pump (22) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1) outside, the first condenser (16) also has the heated medium pipeline to be communicated with outside, the second condenser (17) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (18), the second evaporimeter (19) and the 3rd evaporimeter (23) medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein, during without the second evaporimeter (19), the first condenser (16) has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through first throttle valve (20) to change to the first condenser (16) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20), and the first evaporimeter (18) increases the refrigerant vapour passage and is communicated with the second absorption-generator (4).
7. back-heating type the 3rd class absorption heat pump, described in claim 3, the second absorption-generator has in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the first cryogen liquid pump, the second cryogen liquid pump or the 3rd choke valve, first throttle valve and the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator (5) and to have the refrigerant vapour passage to be communicated with the first condenser (16) in generator (5), the first condenser (16) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20), with first minute steam chest (11) have the refrigerant vapour passage with outside be communicated be defined as first minute steam chest (11) have the refrigerant vapour passage to be communicated with the second condenser (17), the second condenser (17) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) or the second evaporimeter (19) through the first cryogen liquid pump (21), the first evaporimeter (18) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the second choke valve (24), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (19) and to have the refrigerant vapour passage to be communicated with the second absorption-generator (4) in the second absorption-generator (4), to absorb-evaporimeter (1) has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorber (2) absorber (2), absorption-evaporimeter (1) has the refrigerant vapour passage to be communicated with the first absorption-generator (3) to be defined as the first evaporimeter (18) to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second cryogen liquid pump (22) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1) outside, or be defined as the first condenser (16) and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the 3rd choke valve (26) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with, the first condenser (16) also has the heated medium pipeline to be communicated with outside, the second condenser (17) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (18) and the second evaporimeter (19) medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: during 1. without the second evaporimeter (19), the second condenser (17) has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) or the second evaporimeter (19) through the first cryogen liquid pump (21) to be defined as the second condenser (17) and to have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21), cancel the cryogen liquid pipeline that the first evaporimeter (18) is communicated with the second evaporimeter (19) through the second choke valve (24), the first evaporimeter (18) increases the refrigerant vapour passage and is communicated with the second absorption-generator (4); 2. or have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20) the first condenser (16) to be adjusted into the first condenser (16) and to have the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through first throttle valve (20), simultaneously the first evaporimeter (18) being had the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the second choke valve (24) is adjusted into the second evaporimeter (19) and has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the second choke valve (24).
8. back-heating type the 3rd class absorption heat pump, described in claim 3, the second absorption-generator is without in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the first cryogen liquid pump, the first throttle valve, the second cryogen liquid pump or the second choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator (5) and to have the refrigerant vapour passage to be communicated with the first condenser (16) in generator (5), the first condenser (16) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20), with first minute steam chest (11) have the refrigerant vapour passage with outside be communicated be defined as first minute steam chest (11) have the refrigerant vapour passage to be communicated with the second condenser (17), the second condenser (17) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (19) and to have the refrigerant vapour passage to be communicated with the second absorption-generator (4) in the second absorption-generator (4), to absorb-evaporimeter (1) has refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorber (2) absorber (2), absorption-evaporimeter (1) has the refrigerant vapour passage to be communicated with the first absorption-generator (3) to be defined as the first evaporimeter (18) to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second cryogen liquid pump (22) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1) outside, or be defined as the first condenser (16) and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second choke valve (24) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with, the first condenser (16) also has the heated medium pipeline to be communicated with outside, the second condenser (17) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (18) and the second evaporimeter (19) medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: 1. or increase by the 3rd choke valve, the first evaporimeter (18) increases the cryogen liquid pipeline and is communicated with the second evaporimeter (19) through the 3rd choke valve (25), the second condenser (17) is had the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21) again and changes to the second condenser (17) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21); During 2. without the second evaporimeter (19), the second condenser (17) has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21) to change to the second condenser (17) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21), and the first evaporimeter (18) increases the refrigerant vapour passage and is communicated with the second absorption-generator (4).
9. back-heating type the 3rd class absorption heat pump, described in claim 4, the second absorption-generator has in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the first cryogen liquid pump, the second choke valve, the 3rd choke valve, the second cryogen liquid pump or the 4th choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator (5) and to have the refrigerant vapour passage to be communicated with the first condenser (16) in generator (5), the first condenser (16) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through first throttle valve (20), the second evaporimeter (19) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the 3rd choke valve (25), the first evaporimeter (18) also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter (23) through the second choke valve (24), with first minute steam chest (11) have the refrigerant vapour passage with outside be communicated be defined as first minute steam chest (11) have the refrigerant vapour passage to be communicated with the second condenser (17), the second condenser (17) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (19) and to have the refrigerant vapour passage to be communicated with the second absorption-generator (4) in the second absorption-generator (4), to absorb-evaporimeter (1) has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter (23) and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorber (2) absorber (2), absorption-evaporimeter (1) has the refrigerant vapour passage to be communicated with the first absorption-generator (3) to be defined as the first evaporimeter (18) or the second evaporimeter (19) to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second cryogen liquid pump (22) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1) outside, or be defined as the first condenser (16) and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the 4th choke valve (26) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with, the first condenser (16) also has the heated medium pipeline to be communicated with outside, the second condenser (17) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (18), the second evaporimeter (19) and the 3rd evaporimeter (23) medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: 1. or with the first condenser (16) have the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through first throttle valve (20), the second evaporimeter (19) has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the 3rd choke valve (25) to change to the first condenser (16) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20) again, the first evaporimeter (18) or the 3rd evaporimeter (23) have the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the 3rd choke valve (25), have the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21) the second condenser (17) and change to the second condenser (17) and have the cryogen liquid pipeline to be communicated with the second evaporimeter (19) or the first evaporimeter (18) through the first cryogen liquid pump (21); During 2. without the second evaporimeter, the second condenser (17) has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21) to change to the second condenser (17) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21), the first condenser (16) has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through first throttle valve (20), the second evaporimeter (19) has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the 3rd choke valve (25) to change to the first condenser (16) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20) again, and the first evaporimeter (18) increases the refrigerant vapour passage and is communicated with the second absorption-generator (4).
10. back-heating type the 3rd class absorption heat pump, described in claim 4, the second absorption-generator is without in heated medium pipeline and the outside backheating type absorption-generation systems that is communicated with, increase by the first condenser, the second condenser, the first evaporimeter, the second evaporimeter, the 3rd evaporimeter, the first throttle valve, the first cryogen liquid pump, the second choke valve, the second cryogen liquid pump or the 3rd choke valve, there are refrigerant vapour passage and outside the connection to be defined as generator (5) and to have the refrigerant vapour passage to be communicated with the first condenser (16) in generator (5), the first condenser (16) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through first throttle valve (20), the first evaporimeter (18) also has the cryogen liquid pipeline to be communicated with the 3rd evaporimeter (23) through the second choke valve (24), with first minute steam chest (11) have the refrigerant vapour passage with outside be communicated be defined as first minute steam chest (11) have the refrigerant vapour passage to be communicated with the second condenser (17), the second condenser (17) also has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21), there are refrigerant vapour passage and outside the connection to be defined as the second evaporimeter (19) and to have the refrigerant vapour passage to be communicated with the second absorption-generator (4) in the second absorption-generator (4), to absorb-evaporimeter (1) has refrigerant vapour passage and outside the connection to be defined as the 3rd evaporimeter (23) and to have the refrigerant vapour passage to be communicated with absorption-evaporimeter (1), there are refrigerant vapour passage and outside the connection to be defined as the first evaporimeter (18) and to have the refrigerant vapour passage to be communicated with absorber (2) absorber (2), absorption-evaporimeter (1) has the refrigerant vapour passage to be communicated with the first absorption-generator (3) to be defined as the first evaporimeter (18) to have the cryogen liquid pipeline to have the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the second cryogen liquid pump (22) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with again again after having the cryogen liquid pipeline to be communicated with absorption-evaporimeter (1) outside, or be defined as the first condenser (16) and have the cryogen liquid pipeline to have again the refrigerant vapour passage to be communicated with the first absorption-generator (3) through the 3rd choke valve (25) with absorption-evaporimeter (1) after absorption-evaporimeter (1) is communicated with, the first condenser (16) also has the heated medium pipeline to be communicated with outside, the second condenser (17) also has the cooling medium pipeline to be communicated with outside, the first evaporimeter (18), the second evaporimeter (19) and the 3rd evaporimeter (23) medium pipeline that also has surplus heat respectively is communicated with formation single-stage single-action back-heating type the 3rd class absorption heat pump with outside; Wherein: 1. or increase by the 4th choke valve, the first evaporimeter (18) or the 3rd evaporimeter (23) increase the cryogen liquid pipeline and are communicated with the second evaporimeter (19) through the 4th choke valve (26), simultaneously the second condenser (17) are had the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21) and change to the second condenser (17) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21); During 2. without the second evaporimeter (19), the second condenser (17) has the cryogen liquid pipeline to be communicated with the second evaporimeter (19) through the first cryogen liquid pump (21) to change to the second condenser (17) and have the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through the first cryogen liquid pump (21), and the first evaporimeter (18) increases the refrigerant vapour passage and is communicated with the second absorption-generator (4).
11. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 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 the second absorption-generator (4) through newly-increased solution heat exchanger (C), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage parallel double-effect back-heating type the 3rd class absorption heat pump.
12. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-10, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 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 the first solution heat exchanger (9) concentrated solution pipeline afterwards with generator (5) afterwards through newly-increased solution heat exchanger (C), again through the second absorption-generator (4) with first minute steam chest (11) be communicated with, newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage parallel double-effect back-heating type the 3rd class absorption heat pump.
13. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, having the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) in generator (5) is adjusted into generator (5) 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 the second absorption-generator (4) through the first solution heat exchanger (9), having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and the weak solution pipeline is arranged through the first solution pump (6), the first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with generator (5), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
14. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-10, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, with generator (5) have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with and be adjusted into generator (5) and have the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and the weak solution pipeline is arranged through the first solution pump (6), the first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with generator (5), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
15. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 13-14, the second absorption-generator (4) there is the weak solution pipeline through the first solution pump (6), the first solution heat exchanger (9) and newly-increased solution heat exchanger (C) are communicated with generator (5) and are adjusted into the second absorption-generator (4) and have the weak solution pipeline directly to be communicated with generator (5) through newly-increased solution heat exchanger (C) with newly-increased generator (A) connected sum respectively afterwards through the first solution pump (6) and the first solution heat exchanger (9) again, formation single-stage connection in series-parallel economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
16. back-heating type the 3rd class absorption heat pump, in described back-heating type 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, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased generator (A) through the first solution pump (6) and the first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with generator (5) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) in generator (5) is adjusted into generator (5) and has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through newly-increased solution heat exchanger (C) and the first solution heat exchanger (9), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
17. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-10, 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 generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased generator (A) through the first solution pump (6) and the first solution heat exchanger (9), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with generator (5) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), with generator (5) have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with and be adjusted into generator (5) and the concentrated solution pipeline arranged through newly-increased solution heat exchanger (C), the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator release is as the driving thermal medium that increases generator newly, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage series connection economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
18. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 16-17, having the weak solution pipeline to be communicated with newly-increased generator (A) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased generator (A) and generator (5) respectively afterwards through the first solution pump (6) and the first solution heat exchanger (9), form single-stage connection in series-parallel economic benefits and social benefits back-heating type the 3rd class absorption heat pump.
19. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, the first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased the second generator (E) through newly-increased the second solution heat exchanger (G) with newly-increased generator (A) connected sum through newly-increased solution heat exchanger (C) respectively, newly-increased generator (A) also has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through newly-increased solution heat exchanger (C), newly-increased the second generator (E) also has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through newly-increased the second solution heat exchanger (G), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, increasing the second generator (E) newly after newly-increased generator (A) also has refrigerant vapour passage and newly-increased the second generator (E) to be communicated with has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F) again---the driving thermal medium of newly-increased the second generator of refrigerant vapour conduct that newly-increased generator produces, newly-increased the second generator (E) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage triple effect back-heating type in parallel the 3rd class absorption heat pump.
20. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-10, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, the first solution pump (6) is set up the weak solution pipeline and is communicated with newly-increased the second generator (E) through newly-increased the second solution heat exchanger (G) with newly-increased generator (A) connected sum through newly-increased solution heat exchanger (C) respectively, newly-increased generator (A) has the concentrated solution pipeline to have the concentrated solution pipeline all to converge through the first solution heat exchanger (9) concentrated solution pipeline afterwards with generator (5) afterwards through newly-increased the second solution heat exchanger (G) with newly-increased the second generator (E) afterwards through newly-increased solution heat exchanger (C), again through the second absorption-generator (4) with first minute steam chest (11) be communicated with, newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, increasing the second generator (E) newly after newly-increased generator (A) also has refrigerant vapour passage and newly-increased the second generator (E) to be communicated with has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F) again---the driving thermal medium of newly-increased the second generator of refrigerant vapour conduct that newly-increased generator produces, newly-increased the second generator (E) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage triple effect back-heating type in parallel the 3rd class absorption heat pump.
21. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, having the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) in generator (5) is adjusted into generator (5) and has the concentrated solution pipeline to be communicated with newly-increased generator (A) through the first solution heat exchanger (9), newly-increased generator (A) also has the newly-increased solution heat exchanger (C) of concentrated solution pipeline to be communicated with newly-increased the second generator (E), newly-increased the second generator (E) also has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through newly-increased the second solution heat exchanger (G), having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and the weak solution pipeline is arranged through the first solution pump (6), newly-increased the second solution heat exchanger (G), newly-increased solution heat exchanger (C) and the first solution heat exchanger (9) are communicated with generator (5), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, increasing the second generator (E) newly after newly-increased generator (A) also has refrigerant vapour passage and newly-increased the second generator (E) to be communicated with has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F) again---the driving thermal medium of newly-increased the second generator of refrigerant vapour conduct that newly-increased generator produces, newly-increased the second generator (E) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
22. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-10, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger and newly-increased the second solution heat exchanger, with generator (5) have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with and be adjusted into generator (5) and have the concentrated solution pipeline to be communicated with newly-increased generator (A) through the first solution heat exchanger (9), newly-increased generator (A) also has the newly-increased solution heat exchanger (C) of concentrated solution pipeline to be communicated with newly-increased the second generator (E), newly-increased the second generator (E) also have the concentrated solution pipeline through newly-increased the second solution heat exchanger (G) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and the weak solution pipeline is arranged through the first solution pump (6), newly-increased the second solution heat exchanger (G), newly-increased solution heat exchanger (C) and the first solution heat exchanger (9) are communicated with generator (5), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, increasing the second generator (E) newly after newly-increased generator (A) also has refrigerant vapour passage and newly-increased the second generator (E) to be communicated with has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F) again---the driving thermal medium of newly-increased the second generator of refrigerant vapour conduct that newly-increased generator produces, newly-increased the second generator (E) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
23. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-6, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased solution pump and newly-increased the second solution pump, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased the second generator (E) through the first solution pump (6) and the first solution heat exchanger (9), newly-increased the second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased the second solution pump (H) and newly-increased the second solution heat exchanger (G), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with generator (5) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), having the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) in generator (5) is adjusted into generator (5) and the concentrated solution pipeline is arranged through newly-increased solution heat exchanger (C), newly-increased the second solution heat exchanger (G) and the first solution heat exchanger (9) are communicated with the second absorption-generator (4), newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, increasing the second generator (E) newly after newly-increased generator (A) also has refrigerant vapour passage and newly-increased the second generator (E) to be communicated with has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F) again---the driving thermal medium of newly-increased the second generator of refrigerant vapour conduct that newly-increased generator produces, newly-increased the second generator (E) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
24. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-10, increase newly-increased generator, newly-increased the second generator, newly-increased choke valve, newly-increased the second choke valve, newly-increased solution heat exchanger, newly-increased the second solution heat exchanger, newly-increased solution pump and newly-increased the second solution pump, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased the second generator (E) through the first solution pump (6) and the first solution heat exchanger (9), newly-increased the second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased the second solution pump (H) and newly-increased the second solution heat exchanger (G), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with generator (5) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), with generator (5) have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with and be adjusted into generator (5) and the concentrated solution pipeline arranged through newly-increased solution heat exchanger (C), newly-increased the second solution heat exchanger (G), the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, newly-increased generator (A) has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B) again after having the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) to have the refrigerant vapour passage to be communicated with newly-increased generator (A) generator (5)---and the refrigerant vapour of generator generation is as the driving thermal medium that increases generator newly, increasing the second generator (E) newly after newly-increased generator (A) also has refrigerant vapour passage and newly-increased the second generator (E) to be communicated with has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F) again---the driving thermal medium of newly-increased the second generator of refrigerant vapour conduct that newly-increased generator produces, newly-increased the second generator (E) also has the refrigerant vapour passage to be communicated with the first condenser (16), forms single-stage serially connected three-effect back-heating type the 3rd class absorption heat pump.
25. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, to absorb-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8) to be adjusted into absorption-evaporimeter (1) and to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (I) through newly-increased solution heat exchanger (C), newly-increased absorption-evaporimeter (I) also has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8) and newly-increased solution heat exchanger (C), the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (8) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), the first evaporimeter (18) or the second condenser (17) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively again, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
26. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorption-evaporimeter, to absorb-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8) to be adjusted into absorption-evaporimeter (1) and to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (I) through newly-increased solution heat exchanger (C), newly-increased absorption-evaporimeter (I) also has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8) and newly-increased solution heat exchanger (C), the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (8) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), the first evaporimeter (18) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively again, or first condenser (16) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (I) newly after newly-increased absorptions-evaporimeter (I) is communicated with and have again the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively, formation provides one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to absorber.
27. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorption-evaporimeter and newly-increased cryogen liquid pump, there is the weak solution pipeline to be communicated with absorption-evaporimeter (1) to be adjusted into absorber (2) to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (I) through newly-increased solution heat exchanger (C) absorber (2), newly-increased absorption-evaporimeter (I) also has the weak solution pipeline to be communicated with absorption-evaporimeter (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (8) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), the first evaporimeter (18) or the second condenser (17) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively again, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
28. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorption-evaporimeter, there is the weak solution pipeline to be communicated with absorption-evaporimeter (1) to be adjusted into absorber (2) to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (I) through newly-increased solution heat exchanger (C) absorber (2), newly-increased absorption-evaporimeter (I) also has the weak solution pipeline to be communicated with absorption-evaporimeter (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (8) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), the first evaporimeter (18) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively again, or first condenser (16) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (I) newly after newly-increased absorptions-evaporimeter (I) is communicated with and have again the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively, formation provides one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to absorber.
29. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased solution heat exchanger, newly-increased absorption-evaporimeter, newly-increased cryogen liquid pump and newly-increased solution pump, with second minute steam chest (12) have the concentrated solution pipeline to be communicated with absorber (2) to be adjusted into second minute steam chest (12) have the concentrated solution pipeline to be communicated with absorber (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), there is the weak solution pipeline to be communicated with absorption-evaporimeter (1) to be adjusted into absorber (2) to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (I) through newly-increased solution heat exchanger (C) absorber (2), newly-increased absorption-evaporimeter (I) has the weak solution pipeline to be communicated with absorption-evaporimeter (1) again, the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorber (2) to be adjusted into the first evaporimeter (18) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), the first evaporimeter (18) or the second condenser (17) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorber (2) again, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber by newly-increased absorption-evaporimeter.
30. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased solution pump, with second minute steam chest (12) have the concentrated solution pipeline to be communicated with absorber (2) to be adjusted into second minute steam chest (12) have the concentrated solution pipeline to be communicated with absorber (2) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), there is the weak solution pipeline to be communicated with absorption-evaporimeter (1) to be adjusted into absorber (2) to have the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (I) through newly-increased solution heat exchanger (C) absorber (2), newly-increased absorption-evaporimeter (I) has the weak solution pipeline to be communicated with absorption-evaporimeter (1) again, the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorber (2) to be adjusted into the first evaporimeter (18) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), the first evaporimeter (18) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorber (2) again, or first condenser (16) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorption-evaporimeter (I) newly after newly-increased absorptions-evaporimeter (I) is communicated with and have again the refrigerant vapour passage to be communicated with absorber (2), formation provides one generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour by increasing absorption-evaporimeter newly to absorber.
31. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased cryogen liquid pump, newly-increased solution heat exchanger and newly-increased absorber, to absorb-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8) to be adjusted into absorption-evaporimeter (1) and to have the weak solution pipeline to be communicated with newly-increased absorber (K) through the 3rd solution pump (8) and newly-increased solution heat exchanger (C), newly-increased absorber (K) also has the weak solution pipeline to be communicated with the first absorption-generator (3) through newly-increased solution heat exchanger (C), there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter (18) or the second condenser (17) and to set up the cryogen liquid pipeline and have again the refrigerant vapour passage to be communicated with newly-increased absorber (K) through increasing cryogen liquid pump (J) newly and increasing absorber (2) newly after absorber (2) is communicated with absorber (2), newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
32. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, to absorb-evaporimeter (1) has the weak solution pipeline to be communicated with the first absorption-generator (3) through the 3rd solution pump (8) to be adjusted into absorption-evaporimeter (1) and to have the weak solution pipeline to be communicated with newly-increased absorber (K) through the 3rd solution pump (8) and newly-increased solution heat exchanger (C), newly-increased absorber (K) also has the weak solution pipeline to be communicated with the first absorption-generator (3) through newly-increased solution heat exchanger (C), there are heated medium pipeline and outside the connection to be adjusted into the first evaporimeter (18) and to set up the cryogen liquid pipeline and have again the refrigerant vapour passage to be communicated with newly-increased absorber (K) through increasing cryogen liquid pump (J) newly and increasing absorber (2) newly after absorber (2) is communicated with absorber (2), or be adjusted into the first condenser (16) set up the cryogen liquid pipeline through newly-increased choke valve (B) with increase absorber (2) newly after absorber (2) is communicated with and have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
33. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, having the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) in generator (5) is adjusted into generator (5) and has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through the first solution heat exchanger (9), newly-increased absorber (K) also has the weak solution pipeline to be communicated with the second absorption-generator (4) through newly-increased solution heat exchanger (C), having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and the weak solution pipeline is arranged through the first solution pump (6), newly-increased solution heat exchanger (C) and the first solution heat exchanger (9) are communicated with generator (5), with absorber (2) have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter (19) set up the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), or be adjusted into that the first condenser (16) is set up the cryogen liquid pipeline through newly-increased choke valve (B) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber; Wherein, when the second evaporimeter, the second evaporimeter (19) the cryogen liquid pipeline is arranged through newly-increased cryogen liquid pump (J) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K) to change to the first evaporimeter (18) have the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K).
34. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger and newly-increased absorber, with generator (5) have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with and be adjusted into generator (5) and have the concentrated solution pipeline to be communicated with newly-increased absorber (K) through the first solution heat exchanger (9), newly-increased absorber (K) also have the weak solution pipeline through newly-increased solution heat exchanger (C) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and the weak solution pipeline is arranged through the first solution pump (6), newly-increased solution heat exchanger (C) and the first solution heat exchanger (9) are communicated with generator (5), with absorber (2) have the heated medium pipeline with outside is communicated be adjusted into the first evaporimeter (18) have the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), or be adjusted into that the first condenser (16) has the cryogen liquid pipeline through newly-increased choke valve (B) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
35. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, having the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) in generator (5) is adjusted into generator (5) and has the concentrated solution pipeline to be communicated with the second absorption-generator (4) through the first solution heat exchanger (9) and newly-increased solution heat exchanger (C), having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased absorber (K) through the first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (K) also has the weak solution pipeline to be communicated with generator (5) through newly-increased solution pump (D) and the first solution heat exchanger (9), with absorber (2) have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter (19) set up the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), or be adjusted into that the first condenser (16) is set up the cryogen liquid pipeline through newly-increased choke valve (B) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber; Wherein, when the second evaporimeter, the second evaporimeter (19) the cryogen liquid pipeline is arranged through newly-increased cryogen liquid pump (J) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K) to change to the first evaporimeter (18) have the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K).
36. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased solution heat exchanger, newly-increased absorber and newly-increased solution pump, with generator (5) have the concentrated solution pipeline through the first solution heat exchanger (9) and the second absorption-generator (4) with first minute steam chest (11) be communicated with and be adjusted into generator (5) and the concentrated solution pipeline arranged through the first solution heat exchanger (9), newly-increased solution heat exchanger (C) and the second absorption-generator (4) with first minute steam chest (11) be communicated with, having the weak solution pipeline to be communicated with generator (5) through the first solution pump (6) and the first solution heat exchanger (9) in the second absorption-generator (4) is adjusted into the second absorption-generator (4) and has the weak solution pipeline to be communicated with newly-increased absorber (K) through the first solution pump (6) and newly-increased solution heat exchanger (C), newly-increased absorber (K) also has the weak solution pipeline to be communicated with generator (5) through newly-increased solution pump (D) and the first solution heat exchanger (9), with absorber (2) have the heated medium pipeline with outside is communicated be adjusted into the first evaporimeter (18) have the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), or be adjusted into that the first condenser (16) has the cryogen liquid pipeline through newly-increased choke valve (B) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms one generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by absorber.
37. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-10, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator (5) had the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) has the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has respectively refrigerant vapour passage and the first condenser (16) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber by generator.
38. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 5-10, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump, newly-increased absorber, newly-increased condenser and newly-increased choke valve, generator (5) is set up the refrigerant vapour passage and is communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the refrigerant vapour passage to be communicated with newly-increased condenser (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B), newly-increased generator (A) drives in addition the thermal medium pipeline and is communicated with outside, newly-increased absorber (K) and newly-increased condenser (L) also have respectively the heated medium pipeline to be communicated with the outside, and formation is provided respectively double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour to the first condenser and newly-increased absorber by generator.
39. back-heating type the 3rd class absorption heat pump, in claim 5, in described back-heating type the 3rd class absorption heat pump of 7-8, increase newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (18) has the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively, newly-increased generator (A) drives in addition the thermal medium pipeline and is communicated with outside, newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, and formation is by increasing generator newly to absorber or double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour being provided to absorber and absorption-evaporimeter.
40. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 39, 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 (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first evaporimeter (18) through newly-increased choke valve (B), newly-increased condenser (L) also has the heated medium pipeline to be communicated with outside, formation by newly-increased generator respectively to newly-increased condenser and absorber or to newly-increased condenser, absorber and absorption-evaporimeter provide double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour.
41. back-heating type the 3rd class absorption heat pump, described in claim 5, absorption-evaporimeter and the second absorption-generator are without in heated medium pipeline and outside back-heating type the 3rd class absorption heat pump that is communicated with, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator (5) had the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) has the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), with absorber (2) have the heated medium pipeline with outside is communicated be adjusted into the second evaporimeter (19) set up the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), or be adjusted into that the first condenser (16) is set up the cryogen liquid pipeline through newly-increased choke valve (B) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased generator (A) also has respectively refrigerant vapour passage and the first condenser (16) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber jointly by absorber and generator; Wherein, when the second evaporimeter, the second evaporimeter (19) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (J) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K) to change to the first evaporimeter (18) set up the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K).
42. back-heating type the 3rd class absorption heat pump, described in claim 8, absorption-evaporimeter is without in heated medium pipeline and outside back-heating type the 3rd class absorption heat pump that is communicated with, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorber, generator (5) had the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into generator (5) has the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased generator (A) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), with absorber (2) have the heated medium pipeline with outside is communicated be adjusted into the first evaporimeter (18) set up the cryogen liquid pipeline through increase cryogen liquid pump (J) newly and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), or be adjusted into that the first condenser (16) has the cryogen liquid pipeline through newly-increased choke valve (B) and after absorber (2) is communicated with absorber (2) have again the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased generator (A) also has respectively refrigerant vapour passage and the first condenser (16) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to newly-increased absorber jointly by absorber and generator.
43. back-heating type the 3rd class absorption heat pump, in back-heating type the 3rd class absorption heat pump claimed in claim 5, increase newly-increased cryogen liquid pump, newly-increased generator, newly-increased solution heat exchanger, newly-increased solution pump and newly-increased absorption-evaporimeter, the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (18) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), newly-increased absorption-evaporimeter (I) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) 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 (I) through newly-increased solution heat exchanger (C), the first evaporimeter (18) or the second condenser (17) are set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing cryogen liquid pump (J) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorber (2) and absorption-evaporimeter (1) respectively again, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively, newly-increased generator (A) drives in addition the thermal medium pipeline and is communicated with outside, forms by increasing absorption-evaporimeter and newly-increased generator newly jointly to absorber or common double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber and absorption-evaporimeter.
44. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 7-8, increase newly-increased cryogen liquid pump or newly-increased choke valve, newly-increased generator, newly-increased solution heat exchanger, newly-increased absorption-evaporimeter and newly-increased solution pump, the first evaporimeter (18) had the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively to be adjusted into the first evaporimeter (18) has the refrigerant vapour passage to be communicated with newly-increased absorption-evaporimeter (I), newly-increased absorption-evaporimeter (I) also has the weak solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution pump (D) 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 (I) through newly-increased solution heat exchanger (C), the first condenser (16) is set up cryogen liquid pipeline newly-increased absorption-evaporimeter (I) after increasing choke valve (B) newly and newly-increased absorption-evaporimeter (I) is communicated with has the refrigerant vapour passage to be communicated with absorber (2) and absorption-evaporimeter (1) respectively again, or first evaporimeter (18) set up the cryogen liquid pipeline through newly-increased cryogen liquid pump (J) with increase absorption-evaporimeter (I) newly after newly-increased absorption-evaporimeter (I) is communicated with and have again the refrigerant vapour passage to be communicated with absorber (2) and absorption-evaporimeter (1) respectively, newly-increased generator (A) also has the refrigerant vapour passage to be communicated with absorption-evaporimeter (1) and absorber (2) respectively, newly-increased generator (A) drives in addition the thermal medium pipeline and is communicated with outside, forms by increasing absorption-evaporimeter and newly-increased generator newly jointly to absorber or common double-generator two-stage back-heating type the 3rd class absorption heat pump that refrigerant vapour is provided to absorber and absorption-evaporimeter.
45. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 41, increase newly-increased condenser and newly-increased choke valve, to increase generator (A) newly has the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into newly-increased generator (A) and has the refrigerant vapour passage to be communicated with newly-increased condenser (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased choke valve (B), generator (5) and absorber (2) are set up respectively the refrigerant vapour passage and are communicated with the first condenser (16), newly-increased condenser (L) also has the heated medium pipeline to be communicated with outside, and formation is provided respectively double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour jointly to the first condenser and newly-increased absorber by absorber and generator.
46. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 42, increase newly-increased condenser and newly-increased the second choke valve, to increase generator (A) newly has the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into newly-increased generator (A) and has the refrigerant vapour passage to be communicated with newly-increased condenser (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F), generator (5) and absorber (2) are set up respectively the refrigerant vapour passage and are communicated with the first condenser (16), newly-increased condenser (L) also has the heated medium pipeline to be communicated with outside, and formation is provided respectively double-generator two-stage back-heating type the 3rd class absorption heat pump of refrigerant vapour jointly to the first condenser and newly-increased absorber by absorber and generator.
47. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 11-18, increase newly-increased condenser and newly-increased the second choke valve, generator (5) is set up the refrigerant vapour passage and is communicated with newly-increased condenser (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F), newly-increased condenser (L) also has the heated medium pipeline to be communicated with outside, forms single-stage economic benefits and social benefits back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
48. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 19-24, increase newly-increased condenser and newly-increased the 3rd choke valve, generator (5) is set up the refrigerant vapour passage and is communicated with newly-increased condenser (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the 3rd choke valve, newly-increased condenser (L) also has the heated medium pipeline to be communicated with outside, forms single-stage triple effect back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
49. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 19-24, increase 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 condenser (L), newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the 3rd choke valve, newly-increased condenser (L) also has the heated medium pipeline to be communicated with outside, forms single-stage triple effect back-heating type the 3rd class absorption heat pump take newly-increased condenser as additional high-temperature heat supply end.
50. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 47-49, increase newly-increased first flow control valve and newly-increased second adjustable valve, with the first condenser (16) have the heated medium pipeline with outside is communicated be adjusted into the outside and have the heated medium pipeline to be communicated with the first condenser (16) after the first condenser (16) have again the heated medium pipeline to increase second adjustable valve (0) newly with outside connected sum warp and be communicated with newly-increased condenser (L) through increasing first flow choke valve (N) newly respectively, to increase newly condenser (L) have the heated medium pipeline with outside is communicated be adjusted into the first condenser (16) have the heated medium pipeline through newly-increased the second flow throttle valve (O) with increase condenser (L) newly after newly-increased condenser (L) is communicated with and have again the heated medium pipeline to be communicated with the outside, formation adjustable type back-heating type the 3rd class absorption heat pump.
51. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 11-18, increase newly-increased the 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 the first condenser (16) to be adjusted into newly-increased generator (A) and has the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased the second generator (E) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased the second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), newly-increased the second generator (E) also has respectively refrigerant vapour passage and the first condenser (16) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order.
52. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 51, increase newly-increased the second choke valve, to increase newly the second generator (E) have the heated medium pipeline with outside is communicated be adjusted into generator (5) and set up the refrigerant vapour passage and newly-increased the second generator (E) is communicated with after newly-increased the second generator (E) have again the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F)---the refrigerant vapour conduct of generator release increases the driving thermal medium of the second generator newly, two-stage back-heating type three class absorption heat pump of formation take the single-stage economic benefits and social benefits as the first order.
53. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 11-18, increase newly-increased the second generator, newly-increased absorber, newly-increased solution pump, newly-increased solution heat exchanger, newly-increased condenser and newly-increased the second choke valve, newly-increased generator (A) is set up the refrigerant vapour passage and is communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased the second generator (E) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C), newly-increased the second generator (E) also has the concentrated solution pipeline to be communicated with newly-increased absorber (K) through newly-increased solution heat exchanger (C), newly-increased the second generator (E) also has respectively refrigerant vapour passage and newly-increased condenser (L) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the second choke valve (F), newly-increased absorber (K) and newly-increased condenser (L) also have respectively the heated medium pipeline to be communicated with outside, form two-stage back-heating type the 3rd class absorption heat pump take the single-stage economic benefits and social benefits as the first order.
54. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 53, increase newly-increased the 3rd choke valve, to increase newly the second generator (E) have the heated medium pipeline with outside is communicated be adjusted into generator (5) and set up the refrigerant vapour passage and newly-increased the second generator (E) is communicated with after newly-increased the second generator (E) have again the cryogen liquid pipeline to be communicated with newly-increased condenser (L) through newly-increased the 3rd choke valve (M)---the refrigerant vapour conduct of generator release increases the driving thermal medium of the second generator newly, two-stage back-heating type three class absorption heat pump of formation take the single-stage economic benefits and social benefits as the first order.
55. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 19-24, increase newly-increased the 3rd generator, newly-increased absorber, newly-increased solution pump and newly-increased solution heat exchanger, to increase the second generator (E) newly has the refrigerant vapour passage to be communicated with the first condenser (16) to be adjusted into newly-increased the second generator (E) to have the refrigerant vapour passage to be communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased the 3rd generator through newly-increased solution pump (D) 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 (K) through newly-increased solution heat exchanger (C), newly-increased the 3rd generator also has respectively refrigerant vapour passage and the first condenser (16) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased absorber (K) also has the heated medium pipeline to be communicated with outside, forms two-stage back-heating type the 3rd class absorption heat pump take the single-stage triple effect as the first order.
56. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 55, increase newly-increased the 3rd choke valve, to increase newly the 3rd generator have the heated medium pipeline with outside is communicated be adjusted into generator (5) or newly-increased generator (A) and set up the refrigerant vapour passage and newly-increased the 3rd generator is communicated with after newly-increased the 3rd generator have again the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the 3rd choke valve---the refrigerant vapour conduct of generator (5) or newly-increased generator (A) generation increases the driving thermal medium of the 3rd generator, two-stage back-heating type three class absorption heat pump of formation take the single-stage triple effect as the first order newly.
57. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 19-24, 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 3rd choke valve, newly-increased the second generator (E) is set up the refrigerant vapour passage and is communicated with newly-increased absorber (K), newly-increased absorber (K) also has the weak solution pipeline to be communicated with newly-increased the 3rd generator through newly-increased solution pump (D) 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 (K) through newly-increased solution heat exchanger (C), newly-increased the 3rd generator also has respectively refrigerant vapour passage and newly-increased condenser (L) connected sum to have the thermal medium of driving pipeline to be communicated with outside, newly-increased condenser (L) also has the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the 3rd choke valve (M), newly-increased absorber (K) and newly-increased condenser (L) also have respectively the heated medium pipeline to be communicated with outside, form two-stage back-heating type the 3rd class absorption heat pump take the single-stage triple effect as the first order.
58. back-heating type the 3rd class absorption heat pump, in described back-heating type the 3rd class absorption heat pump of claim 57, increase newly-increased the 4th choke valve, to increase newly the 3rd generator have the heated medium pipeline with outside is communicated be adjusted into generator (5) or newly-increased generator (A) and set up the refrigerant vapour passage and newly-increased the 3rd generator is communicated with after newly-increased the 3rd generator have again the cryogen liquid pipeline to be communicated with the first condenser (16) through newly-increased the 4th choke valve---the refrigerant vapour conduct of generator (5) or newly-increased generator (A) generation increases the driving thermal medium of the 3rd generator, two-stage back-heating type three class absorption heat pump of formation take the single-stage triple effect as the first order newly.
CN2010106219230A 2010-12-28 2010-12-28 Regenerative absorption-generation system and regenerative third-type absorption heat pump Active CN102072583B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010106219230A CN102072583B (en) 2010-12-28 2010-12-28 Regenerative absorption-generation system and regenerative third-type absorption heat pump

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010106219230A CN102072583B (en) 2010-12-28 2010-12-28 Regenerative absorption-generation system and regenerative third-type absorption heat pump

Publications (2)

Publication Number Publication Date
CN102072583A CN102072583A (en) 2011-05-25
CN102072583B true CN102072583B (en) 2013-03-20

Family

ID=44031228

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010106219230A Active CN102072583B (en) 2010-12-28 2010-12-28 Regenerative absorption-generation system and regenerative third-type absorption heat pump

Country Status (1)

Country Link
CN (1) CN102072583B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012088650A1 (en) * 2010-12-31 2012-07-05 Li Huayu Regenerative absorbing/generating system and regenerative third-type absorption heat pump
WO2013003982A1 (en) * 2011-07-06 2013-01-10 Li Huayu Third-type absorption heat pump
CN102353173B (en) * 2011-09-12 2013-11-20 李华玉 Classified generation third-class absorption heat pump
CN102538277B (en) * 2011-12-11 2014-06-25 李华玉 Third-class absorption heat pump with regenerative heat supply end
CN102706027B (en) * 2012-04-01 2014-07-30 李华玉 Double-effect regeneration absorption-generation system and regeneration third-class absorption heat pump
CN102635971B (en) * 2012-04-09 2014-06-25 李华玉 Double-effect heat-recovering absorbing-generating system and heat-recovering third-class absorption heat pump
CN102679612B (en) * 2012-05-14 2014-07-30 李华玉 Fractional condensation third-class absorption type heat pump
CN113418320B (en) * 2021-06-16 2023-07-28 郑喜勋 Device for raising low-temperature heat source temperature and application method thereof

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6311504B1 (en) * 1999-03-30 2001-11-06 Sanyo Electric Co., Ltd. Absorption heat pump and method for controlling the same
CN1877227A (en) * 2006-05-13 2006-12-13 李华玉 Two-stage type-I absorption heat pump
CN101586891A (en) * 2009-02-27 2009-11-25 李华玉 Regenerative generation-absorption system and high temperature second absorption heat pump
CN101799222A (en) * 2009-02-27 2010-08-11 李华玉 Regenerative generating-absorbing system and regenerative second-type absorbing heat pump

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004257705A (en) * 2003-02-27 2004-09-16 Sanyo Electric Co Ltd Concentration device using absorption heat pump

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6311504B1 (en) * 1999-03-30 2001-11-06 Sanyo Electric Co., Ltd. Absorption heat pump and method for controlling the same
CN1877227A (en) * 2006-05-13 2006-12-13 李华玉 Two-stage type-I absorption heat pump
CN101586891A (en) * 2009-02-27 2009-11-25 李华玉 Regenerative generation-absorption system and high temperature second absorption heat pump
CN101799222A (en) * 2009-02-27 2010-08-11 李华玉 Regenerative generating-absorbing system and regenerative second-type absorbing heat pump

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
JP特开2004-257705A 2004.09.16

Also Published As

Publication number Publication date
CN102072583A (en) 2011-05-25

Similar Documents

Publication Publication Date Title
CN102072583B (en) Regenerative absorption-generation system and regenerative third-type absorption heat pump
CN102095273B (en) Double generation-diabsorption system and backheating type second absorption heat pump
CN102116538B (en) Double-effect and triple-effect first-type absorption heat pump with heat return end and heat supply end
CN101004303B (en) Three-level first category absorption heat pump
CN101586891B (en) Regenerative generation-absorption system and high temperature second absorption heat pump
CN102042712A (en) Backheating type absorption-generation system and multiterminal heat-supply third-class absorption heat pump
CN101979936B (en) Recuperative generation-absorption system and recuperative first-type absorption heat pump
CN101957092A (en) Type III absorbing and generating system and type III absorbing heat pump
CN101957093B (en) Absorption-reabsorption-generation system and first-class absorption heat pump
CN103851823B (en) Compound generation first-class absorption type heat pump
CN101458006A (en) Method for enhancing first kind absorption heat pump heat supply temperature and high temperature heat pump
CN101266086B (en) Composite absorption heat pump of second type
CN102287961B (en) Three-generating-three-absorbing system and third-kind absorption-type heat pump
CN102183103A (en) Class III generation-absorption system and regenerative class III absorption heat pump
CN102102919B (en) Back-heating type two-stage absorption-generation systems and back-heating type the 3rd class absorption heat pump
CN103017398A (en) Multi-effect first-class absorption heat pump
CN103148631B (en) Compound generation first-class absorption type heat pump
CN102338498B (en) Staged-generation type first absorption heat pump
CN102706026B (en) Double-effect regenerative absorption-generation system and regenerative first class absorption heat pump
CN102425878B (en) Third type absorption-generation system and regenerative third type absorption heat pump
CN102353172B (en) Backheating double-effect and triple-effect second-type absorption heat pumps
CN102305489A (en) Compound first-class absorption heat pump based on single-effect flow
CN102706027B (en) Double-effect regeneration absorption-generation system and regeneration third-class absorption heat pump
CN103148630B (en) Composite-generationsecond second kind absorption type heat pump
CN102252448A (en) Third generator-absorber system and third absorption heat pump

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant