CN102607209B - Third type absorption heat pump with afterheat double-effect driving function - Google Patents

Third type absorption heat pump with afterheat double-effect driving function Download PDF

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CN102607209B
CN102607209B CN201210059126.7A CN201210059126A CN102607209B CN 102607209 B CN102607209 B CN 102607209B CN 201210059126 A CN201210059126 A CN 201210059126A CN 102607209 B CN102607209 B CN 102607209B
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generator
communicated
solution
heat exchanger
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CN102607209A (en
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李华玉
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    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00—Adapting or protecting infrastructure or their operation
    • Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62—Absorption based systems

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Abstract

The invention provides a third type absorption heat pump with an afterheat double-effect driving function, belonging to the technical field of heat pumps. Solution circulation is formed by an absorber, a third solution heat exchanger, an absorption-generator, a first solution pump, a first solution heat exchanger, a first generator, a steam bleeding chamber, a second generator, a second solution pump and a second solution heat exchanger; wherein the first generator provides refrigerant steam to a first condenser; the steam bleeding chamber provides refrigerant steam to the second generator; the second generator provides refrigerant steam to a second condenser; the first condenser provides refrigerant solution to an evaporator through a throttling valve, the second condenser provides refrigerant solution to the evaporator through a a refrigerant solution pump, and the second generator provides refrigerant solution to the evaporator through a second refrigerant solution pump; the evaporator provides refrigerant solution to a second evaporator through a second throttling valve; the evaporator and the second evaporator respectively provide refrigerant steam to the absorber and the absorption-generator; a second absorber and the first condenser or the absorption-generator supply heat; and the second condenser releases low-temperature heat; therefore, the third type absorption heat pump with the afterheat double-effect driving function is formed.

Description

The 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive
Technical field:
The invention belongs to low temperature heat technical field of heat pumps.
Background technology:
In the 3rd class absorption heat pump, when thering is the larger temperature difference between waste heat supply temperature and environment temperature, should consider the waste heat of solution to drive generating process to adopt double-effect process, to improve the utilization rate of residual heat resources.Waste heat drives while adopting different parts, and the concrete double-effect process that waste heat drives is thereupon different from the annexation between other flow process.For take absorption-generator as waste heat drives the 3rd class absorption heat pump of generation part, mainly increase by the second generator, absorptions-generator and the second generator formation economic benefits and social benefits structure, obtain have surplus heat the 3rd class absorption heat pump of economic benefits and social benefits driving of a series of bands.
Summary of the invention:
Main purpose of the present invention is to provide the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, and concrete summary of the invention subitem is described below:
1. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger and a minute steam chest, absorber has weak solution pipeline to be communicated with absorption-generator, absorption-generator also has weak solution pipeline to be communicated with the first generator through the first solution pump and the first solution heat exchanger, the first generator also has concentrated solution pipeline to be communicated with a minute steam chest through the first solution heat exchanger and absorption-generator, divide steam chest to also have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with absorber through the second solution pump and the second solution heat exchanger, the first generator also has refrigerant vapour passage to be communicated with the first condenser, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through choke valve, after dividing steam chest to also have refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter or to be communicated with the second condenser through the second choke valve through the second cryogen liquid pump again, the second generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant vapour passage to be communicated with absorber and absorption-generator respectively, the first generator drives thermal medium pipeline to be communicated with outside in addition, absorption-generator or in addition heated medium pipeline are communicated with outside, absorber and the first condenser also have respectively heated medium pipeline to be communicated with outside, the second condenser also has cooling medium pipeline to be communicated with outside, the evaporimeter medium pipeline that also has surplus heat is communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
2. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second choke valve, the second cryogen liquid pump or the 3rd choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and a minute steam chest, absorber has weak solution pipeline to be communicated with absorption-generator through the 3rd solution heat exchanger, absorption-generator also has weak solution pipeline to be communicated with the first generator through the first solution pump and the first solution heat exchanger, the first generator also has concentrated solution pipeline to be communicated with a minute steam chest through the first solution heat exchanger and absorption-generator, divide steam chest to also have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with absorber, the first generator also has refrigerant vapour passage to be communicated with the first condenser, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through choke valve, after dividing steam chest to also have refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter or to be communicated with the second condenser through the 3rd choke valve through the second cryogen liquid pump again, the second generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve, evaporimeter also has refrigerant vapour passage to be communicated with absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with absorption-generator, the first generator drives thermal medium pipeline to be communicated with outside in addition, absorption-generator or in addition heated medium pipeline are communicated with outside, absorber and the first condenser also have respectively heated medium pipeline to be communicated with outside, the second condenser also has cooling medium pipeline to be communicated with outside, evaporimeter and the second evaporimeter medium pipeline that also has surplus heat is respectively communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
3. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, the second generator, the 3rd generator, absorption-generator, absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger, the 4th solution heat exchanger and a minute steam chest, absorber has weak solution pipeline to be communicated with absorption-generator through the 4th solution heat exchanger, absorption-generator also has weak solution pipeline through the first solution pump, the 3rd solution heat exchanger and the first solution heat exchanger are communicated with the first generator, the first generator also has concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with a minute steam chest through the 3rd solution heat exchanger and absorption-generator, divide steam chest to also have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with absorber through the second solution pump and the second solution heat exchanger, absorber also has weak solution pipeline to be communicated with the second absorber through the 3rd solution pump and the 4th solution heat exchanger, the first generator also has refrigerant vapour passage to be communicated with the first condenser, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through choke valve, after dividing steam chest to also have refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter or to be communicated with the second condenser through the second choke valve through the second cryogen liquid pump again, the second generator also has refrigerant vapour passage to be communicated with the second condenser, the 3rd generator also has refrigerant vapour passage to be communicated with the second absorber, the second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant vapour passage to be communicated with absorber and absorption-generator respectively, the first generator and the 3rd generator also have respectively the thermal medium of driving pipeline to be communicated with outside, absorption-generator or in addition heated medium pipeline are communicated with outside, absorber, the first condenser and the second absorber also have respectively heated medium pipeline to be communicated with outside, the second condenser also has cooling medium pipeline to be communicated with outside, the evaporimeter medium pipeline that also has surplus heat is communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
4. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, mainly by the first generator, the second generator, the 3rd generator, absorption-generator, absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, cryogen liquid pump, choke valve, the second choke valve, the second cryogen liquid pump or the 3rd choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger, the 4th solution heat exchanger, the 5th solution heat exchanger and a minute steam chest form, absorber has weak solution pipeline to be communicated with absorption-generator through the 5th solution heat exchanger and the 4th solution heat exchanger, absorption-generator also has weak solution pipeline through the first solution pump, the 3rd solution heat exchanger and the first solution heat exchanger are communicated with the first generator, the first generator also has concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger, the 3rd generator also has concentrated solution pipeline to be communicated with a minute steam chest through the 3rd solution heat exchanger and absorption-generator, divide steam chest to also have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through the second solution pump, the second solution heat exchanger and the 4th solution heat exchanger are communicated with absorber, absorber also has weak solution pipeline to be communicated with the second absorber through the 3rd solution pump and the 5th solution heat exchanger, the first generator also has refrigerant vapour passage to be communicated with the first condenser, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through choke valve, after dividing steam chest to also have refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter or to be communicated with the second condenser through the 3rd choke valve through the second cryogen liquid pump again, the second generator also has refrigerant vapour passage to be communicated with the second condenser, the 3rd generator also has refrigerant vapour passage to be communicated with the second absorber, the second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has cryogen liquid pipeline to be communicated with the second evaporimeter through the second choke valve, evaporimeter also has refrigerant vapour passage to be communicated with absorber, the second evaporimeter also has refrigerant vapour passage to be communicated with absorption-generator, the first generator and the 3rd generator also have respectively the thermal medium of driving pipeline to be communicated with outside, absorption-generator or in addition heated medium pipeline are communicated with outside, absorber, the first condenser and the second absorber also have respectively heated medium pipeline to be communicated with outside, the second condenser also has cooling medium pipeline to be communicated with outside, evaporimeter and the second evaporimeter medium pipeline that also has surplus heat is respectively communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
5. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger, solution choke valve and a minute steam chest, absorber has weak solution pipeline to be communicated with a minute steam chest through solution choke valve and absorption-generator, divide steam chest to also have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline to be communicated with absorber through the second solution pump and the second solution heat exchanger, absorption-generator also has weak solution pipeline to be communicated with the first generator through the first solution pump and the first solution heat exchanger, the first generator also has concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger, the first generator also has refrigerant vapour passage to be communicated with the first condenser, the first condenser also has cryogen liquid pipeline to be communicated with evaporimeter through choke valve, after dividing steam chest to also have refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter or to be communicated with the second condenser through the second choke valve through the second cryogen liquid pump again, the second generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant vapour passage to be communicated with absorber and absorption-generator respectively, the first generator drives thermal medium pipeline to be communicated with outside in addition, absorption-generator or in addition heated medium pipeline are communicated with outside, absorber and the first condenser also have respectively heated medium pipeline to be communicated with outside, the second condenser also has cooling medium pipeline to be communicated with outside, the evaporimeter medium pipeline that also has surplus heat is communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
6. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and a minute steam chest, absorber has weak solution pipeline to be communicated with a minute steam chest through the 3rd solution heat exchanger and absorption-generator, divide steam chest to also have concentrated solution pipeline to be communicated with the second generator through the second solution heat exchanger, the second generator also has concentrated solution pipeline through the second solution pump, the second solution heat exchanger and the 3rd solution heat exchanger are communicated with absorber, absorption-generator also has weak solution pipeline to be communicated with the first generator through the first solution pump and the first solution heat exchanger, the first generator also has concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger, the first generator also has refrigerant vapour passage to be communicated with the first condenser, the first condenser also has cryogen liquid pipeline to be communicated with the second evaporimeter through choke valve, the second evaporimeter also has refrigerant vapour passage to be communicated with absorption-generator, after dividing steam chest to also have refrigerant vapour passage to be communicated with the second generator, the second generator has cryogen liquid pipeline to be communicated with evaporimeter or to be communicated with the second condenser through the second choke valve through the second cryogen liquid pump again, the second generator also has refrigerant vapour passage to be communicated with the second condenser, the second condenser also has cryogen liquid pipeline to be communicated with evaporimeter through cryogen liquid pump, evaporimeter also has refrigerant vapour passage to be communicated with absorber, the first generator drives thermal medium pipeline to be communicated with outside in addition, absorption-generator or in addition heated medium pipeline are communicated with outside, absorber and the first condenser also have respectively heated medium pipeline to be communicated with outside, the second condenser also has cooling medium pipeline to be communicated with outside, evaporimeter and the second evaporimeter medium pipeline that also has surplus heat is respectively communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
7. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the band described in the 5th, increase by the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, there is weak solution pipeline to be communicated with the first generator and to be adjusted into absorption-generator and to have weak solution pipeline to be communicated with the second absorber through the first solution pump and the 3rd solution heat exchanger through the first solution pump and the first solution heat exchanger in absorption-generator, the second absorber has weak solution pipeline to be communicated with the first generator through the 3rd solution pump and the first solution heat exchanger again, the first generator is had concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger to be adjusted into the first generator has concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with absorption-generator through the 3rd solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the second absorber, the 3rd generator drives thermal medium pipeline to be communicated with outside in addition, the second absorber also has heated medium pipeline to be communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
8. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the band described in the 6th, increase by the 3rd generator, the second absorber, the 3rd solution pump and the 4th solution heat exchanger, there is weak solution pipeline to be communicated with the first generator and to be adjusted into absorption-generator and to have weak solution pipeline to be communicated with the second absorber through the first solution pump and the 4th solution heat exchanger through the first solution pump and the first solution heat exchanger in absorption-generator, the second absorber has weak solution pipeline to be communicated with the first generator through the 3rd solution pump and the first solution heat exchanger again, the first generator is had concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger to be adjusted into the first generator has concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger, the 3rd generator has concentrated solution pipeline to be communicated with absorption-generator through the 4th solution heat exchanger again, the 3rd generator also has refrigerant vapour passage to be communicated with the second absorber, the 3rd generator drives thermal medium pipeline to be communicated with outside in addition, the second absorber also has heated medium pipeline to be communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
9. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 1-2 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first solution pump is set up weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with a minute steam chest through newly-increased solution heat exchanger and absorption-generator, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
10. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 1-2 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with the first generator and to be adjusted into absorption-generator and to have weak solution pipeline through the first solution pump through the first solution pump and the first solution heat exchanger in absorption-generator, the first solution heat exchanger and newly-increased solution heat exchanger are communicated with the first generator, the first generator is had concentrated solution pipeline to be communicated with a minute steam chest through the first solution heat exchanger and absorption-generator to be adjusted into the first generator has concentrated solution pipeline to be communicated with newly-increased generator through increasing solution heat exchanger newly, newly-increased generator has concentrated solution pipeline to be communicated with a minute steam chest through the first solution heat exchanger and absorption-generator again, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
11. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 1-2 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the first generator and to be adjusted into absorption-generator and to have weak solution pipeline to be communicated with newly-increased generator through the first solution pump and the first solution heat exchanger through the first solution pump and the first solution heat exchanger in absorption-generator, newly-increased generator has concentrated solution pipeline to be communicated with the first generator through newly-increased solution pump and newly-increased solution heat exchanger again, the first generator there is is concentrated solution pipeline to be communicated with a minute steam chest through the first solution heat exchanger and absorption-generator to be adjusted into the first generator and have concentrated solution pipeline through increasing solution heat exchanger newly, the first solution heat exchanger and absorption-generator are communicated with a minute steam chest, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
12. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 3-4 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, absorption-generator is had to weak solution pipeline through the first solution pump, the 3rd solution heat exchanger and the first solution heat exchanger are communicated with the first generator and are adjusted into absorption-generator and have weak solution pipeline through the first solution heat exchanger, to be communicated with the first generator connected sum through increasing solution heat exchanger newly with newly-increased generator more respectively after the first solution pump and the 3rd solution heat exchanger again, newly-increased generator also has concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
13. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 3-4 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, absorption-generator is had to weak solution pipeline through the first solution pump, the 3rd solution heat exchanger and the first solution heat exchanger are communicated with the first generator and are adjusted into absorption-generator and have weak solution pipeline through the first solution pump, the 3rd solution heat exchanger, the first solution heat exchanger and newly-increased solution heat exchanger are communicated with the first generator, there is concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger in the first generator, newly-increased generator has concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger again, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
14. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 3-4 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, absorption-generator is had to weak solution pipeline through the first solution pump, the 3rd solution heat exchanger and the first solution heat exchanger are communicated with the first generator and are adjusted into absorption-generator and have weak solution pipeline through the first solution pump, the 3rd solution heat exchanger and the first solution heat exchanger are communicated with newly-increased generator, newly-increased generator has concentrated solution pipeline to be communicated with the first generator through newly-increased solution pump and newly-increased solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger and the first solution heat exchanger in the first generator, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
15. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 5-6 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first solution pump is set up weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
16. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 5-6 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with the first generator and to be adjusted into absorption-generator and to have weak solution pipeline through the first solution pump through the first solution pump and the first solution heat exchanger in absorption-generator, the first solution heat exchanger and newly-increased solution heat exchanger are communicated with the first generator, there is concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger in the first generator, newly-increased generator has concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger again, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
17. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 5-6 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the first generator and to be adjusted into absorption-generator and to have weak solution pipeline to be communicated with newly-increased generator through the first solution pump and the first solution heat exchanger through the first solution pump and the first solution heat exchanger in absorption-generator, newly-increased generator has concentrated solution pipeline to be communicated with the first generator through newly-increased solution pump and newly-increased solution heat exchanger again, there is concentrated solution pipeline to be communicated with absorption-generator through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with absorption-generator through newly-increased solution heat exchanger and the first solution heat exchanger in the first generator, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
18. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 7-8 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 3rd solution pump is set up weak solution pipeline and is communicated with newly-increased generator through newly-increased solution heat exchanger, newly-increased generator also has concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
19. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 7-8 item, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with the first generator and to be adjusted into the second absorber and to have weak solution pipeline through the 3rd solution pump through the 3rd solution pump and the first solution heat exchanger the second absorber, the first solution heat exchanger and newly-increased solution heat exchanger are communicated with the first generator, there is concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with newly-increased generator through newly-increased solution heat exchanger in the first generator, newly-increased generator has concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger again, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
20. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in 7-8 item, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the first generator and to be adjusted into the second absorber and to have weak solution pipeline to be communicated with newly-increased generator through the 3rd solution pump and the first solution heat exchanger through the 3rd solution pump and the first solution heat exchanger the second absorber, newly-increased generator has concentrated solution pipeline to be communicated with the first generator through newly-increased solution pump and newly-increased solution heat exchanger again, there is concentrated solution pipeline to be communicated with the 3rd generator through the first solution heat exchanger to be adjusted into the first generator to have concentrated solution pipeline to be communicated with the 3rd generator through newly-increased solution heat exchanger and the first solution heat exchanger in the first generator, after having refrigerant vapour passage to be communicated with the first condenser to be adjusted into the first generator to have refrigerant vapour passage to be communicated with newly-increased generator in the first generator, newly-increased generator has cryogen liquid pipeline to be communicated with the first condenser through newly-increased choke valve again, newly-increased generator also has refrigerant vapour passage to be communicated with the first condenser, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
21. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, at 12-14, arbitrary band described in 18-20 item has surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, cancel the 3rd generator and the outside driving thermal medium pipeline being communicated with, increase newly-increased the second choke valve, the first generator set up refrigerant vapour passage and be communicated with the 3rd generator after the 3rd generator have again cryogen liquid pipeline to be communicated with the first condenser through newly-increased the second choke valve---the first generator provides refrigerant vapour to make its driving thermal medium to the 3rd generator, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
The 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive shown in Fig. 1 of take is below the present invention of example brief description:
In Fig. 1, the refrigerant vapour that minute steam chest 15 discharges directly provides to the second condenser 6, but is used as the driving thermal medium of the second generator 2, and this brings following effect:
(1) after the refrigerant vapour (waste heat) that evaporimeter 7 provides to absorption-generator 3 is absorbed by solution, its heat release part provides to heated medium, and another part is for the generating process of solution; When absorption-generator 3 is without heated medium pipeline during with outside connection, the entrained waste heat of this part refrigerant vapour is almost all for the generating process of solution.
(2) it is born that the refrigerant vapour that divides steam chest 15 to discharge is that the solution of flowing through in absorptions-generator 3 issues at waste-heat, is used as the solution generating process of the second generator 2, be waste heat for the second time for the heating process of solution, realize waste heat double-effect process.
(3) thermic load occurring for solution in absorption-generator 3 can regulate as required, and absorption-generator 3 and the second generator 2 economic benefits and social benefits thermic loads regulate thereupon.
Accompanying drawing explanation:
Fig. 1 is according to band provided by the present invention the 3rd class absorption heat pump the 1st kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 2 is according to band provided by the present invention the 3rd class absorption heat pump the 2nd kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 3 is according to band provided by the present invention the 3rd class absorption heat pump the 3rd kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 4 is according to band provided by the present invention the 3rd class absorption heat pump the 4th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 5 is according to band provided by the present invention the 3rd class absorption heat pump the 5th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 6 is according to band provided by the present invention the 3rd class absorption heat pump the 6th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 7 is according to band provided by the present invention the 3rd class absorption heat pump the 7th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 8 is according to band provided by the present invention the 3rd class absorption heat pump the 8th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Fig. 9 is according to band provided by the present invention the 3rd class absorption heat pump the 9th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Figure 10 is according to band provided by the present invention the 3rd class absorption heat pump the 10th kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Figure 11 is according to band provided by the present invention the 3rd class absorption heat pump the 11st kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
Figure 12 is according to band provided by the present invention the 3rd class absorption heat pump the 12nd kind of structure and the schematic flow sheet that economic benefits and social benefits drive that have surplus heat.
In figure, 1-the first generator, 2-the second generator, 3-absorption-generator, 4-absorber, 5-the first condenser, 6-the second condenser, 7-evaporimeter, 8-the first solution pump, 9-the second solution pump, 10-cryogen liquid pump, 11-choke valve, 12-the second cryogen liquid pump, 13-the first solution heat exchanger, 14-the second solution heat exchanger, 15-divides steam chest, 16-the second evaporimeter, 17-the second choke valve, 18-the 3rd solution heat exchanger, 19-the 3rd generator, 20-the second absorber, 21-the 3rd solution pump, 22-the 4th solution heat exchanger, 23-the 3rd choke valve, 24-the 5th solution heat exchanger, 25-solution choke valve, A-increases generator newly, and B-increases solution pump newly, and C-increases choke valve newly, and D-increases solution heat exchanger newly, and E-increases the second choke valve newly.
Here it is to be noted: in Figure 11, when the refrigerant vapour pressure of the 3rd generator 19 is during higher than the refrigerant vapour pressure of newly-increased generator A, the concentrated solution outlet of newly-increased generator A can increase solution pump or utilize gravity pressure reduction.
The specific embodiment:
First be noted that in the statement of structure and flow process, in inessential situation, do not repeat; Apparent flow process is not explained.Below in conjunction with accompanying drawing and example, describe the present invention in detail.
Band shown in Fig. 1 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, it is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump, the first solution heat exchanger, the second solution heat exchanger and a minute steam chest, absorber 4 has weak solution pipeline to be communicated with absorption-generator 3, absorption-generator 3 also has weak solution pipeline to be communicated with the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, the first generator 1 also has concentrated solution pipeline to be communicated with a minute steam chest 15 through the first solution heat exchanger 13 and absorption-generator 3, divide steam chest 15 to also have concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 14, the second generator 2 also has concentrated solution pipeline to be communicated with absorber 4 through the second solution pump 9 and the second solution heat exchanger 14, the first generator 1 also has refrigerant vapour passage to be communicated with the first condenser 5, the first condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 11, after dividing steam chest 15 to also have refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through the second cryogen liquid pump 12, the second generator 2 also has refrigerant vapour passage to be communicated with the second condenser 6, the second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 10, evaporimeter 7 also has refrigerant vapour passage to be communicated with absorber 4 and absorption-generator 3 respectively, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorption-generator 3 also has heated medium pipeline to be communicated with outside, absorber 4 and the first condenser 5 also have respectively heated medium pipeline to be communicated with outside, the second condenser 6 also has cooling medium pipeline to be communicated with outside, evaporimeter 7 medium pipeline that also has surplus heat is communicated with outside.
2. in flow process, the weak solution of absorber 4 enters absorption-generator 3, absorb the refrigerant vapour of flash-pot 7 and respectively heat release in heated medium and the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 enters the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, drive heat medium flow through the first generator 1, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of the first generator 1 absorption-generator 3 of flowing through again after the first solution heat exchanger 13, after heat absorbing part vaporization, enter minute steam chest 15, the refrigerant vapour that divides steam chest 15 to discharge offers the second generator 2 and makes its driving thermal medium, divide the concentrated solution of steam chest 15 to enter the second generator 2 through the second solution heat exchanger 14, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 6, the concentrated solution of the second generator 2 enters absorber 4 through the second solution pump 9 and the second solution heat exchanger 14, absorb the refrigerant vapour of flash-pot 7 heat release in heated medium, the refrigerant vapour heat release of the second generator 2 of flowing through becomes cryogen liquid, through the second cryogen liquid pump 12 pressurizations, enter evaporimeter 7 again, the refrigerant vapour heat release of the first condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 5 enters evaporimeter 7 through choke valve 11 throttlings, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 6 enters evaporimeter 7 through 10 pressurizations of cryogen liquid pump, the cryogen liquid that waste heat MEDIA FLOW enters in it through evaporimeter 7, heating becomes refrigerant vapour and respectively to absorption-generator 3 and absorber 4, forms the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 2 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, it is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second choke valve, the second cryogen liquid pump, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and a minute steam chest, absorber 4 has weak solution pipeline to be communicated with absorption-generator 3 through the 3rd solution heat exchanger 18, absorption-generator 3 also has weak solution pipeline to be communicated with the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, the first generator 1 also has concentrated solution pipeline to be communicated with a minute steam chest 15 through the first solution heat exchanger 13 and absorption-generator 3, divide steam chest 15 to also have concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 14, the second generator 2 also has concentrated solution pipeline through the second solution pump 9, the second solution heat exchanger 14 and the 3rd solution heat exchanger 18 are communicated with absorber 4, the first generator 1 also has refrigerant vapour passage to be communicated with the first condenser 5, the first condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 11, after dividing steam chest 15 to also have refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 7 through the second cryogen liquid pump 12 again, the second generator 2 also has refrigerant vapour passage to be communicated with the second condenser 6, the second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 10, evaporimeter 7 also has cryogen liquid pipeline to be communicated with the second evaporimeter 16 through the second choke valve 17, evaporimeter 7 also has refrigerant vapour passage to be communicated with absorber 4, the second evaporimeter 16 also has refrigerant vapour passage to be communicated with absorption-generator 3, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorption-generator 3 also has heated medium pipeline to be communicated with outside, absorber 4 and the first condenser 5 also have respectively heated medium pipeline to be communicated with outside, the second condenser 6 also has cooling medium pipeline to be communicated with outside, evaporimeter 7 and the second evaporimeter 16 medium pipeline that also has surplus heat is respectively communicated with outside.
2. in flow process, the weak solution of absorber 4 enters absorption-generator 3 through the 3rd solution heat exchanger 18, absorption from the refrigerant vapour of the second evaporimeter 16 and respectively heat release in heated medium and the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 enters the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, drive heat medium flow through the first generator 1, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of the first generator 1 absorption-generator 3 of flowing through again after the first solution heat exchanger 13, after heat absorbing part vaporization, enter minute steam chest 15, the refrigerant vapour that divides steam chest 15 to discharge offers the second generator 2 and makes its driving thermal medium, divide the concentrated solution of steam chest 15 to enter the second generator 2 through the second solution heat exchanger 14, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 6, the concentrated solution of the second generator 2 is through the second solution pump 9, the second solution heat exchanger 14 and the 3rd solution heat exchanger 18 enter absorber 4, absorb the refrigerant vapour of flash-pot 7 heat release in heated medium, the refrigerant vapour heat release of the second generator 2 of flowing through becomes cryogen liquid, through the second cryogen liquid pump 12 pressurizations, enter evaporimeter 7 again, the refrigerant vapour heat release of the first condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 5 enters evaporimeter 7 through choke valve 11 throttlings, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 6 enters evaporimeter 7 through 10 pressurizations of cryogen liquid pump, the cryogen liquid of evaporimeter 7 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to absorber 4, second tunnel the second choke valve 17 throttlings enter the second evaporimeter 16, absorbing waste heat becomes refrigerant vapour and provides to absorption-generator 3, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 3 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, it is mainly comprised of the first generator, the second generator, the 3rd generator, absorption-generator, absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, cryogen liquid pump, choke valve, the second choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger, the 4th solution heat exchanger and a minute steam chest, absorber 4 has weak solution pipeline to be communicated with absorption-generator 3 through the 4th solution heat exchanger 22, absorption-generator 3 also has weak solution pipeline through the first solution pump 8, the 3rd solution heat exchanger 18 and the first solution heat exchanger 13 are communicated with the first generator 1, the first generator 1 also has concentrated solution pipeline to be communicated with the 3rd generator 19 through the first solution heat exchanger 13, the 3rd generator 19 also has concentrated solution pipeline to be communicated with a minute steam chest 15 through the 3rd solution heat exchanger 18 and absorption-generator 3, divide steam chest 15 to also have concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 14, the second generator 2 also has concentrated solution pipeline to be communicated with absorber 4 through the second solution pump 9 and the second solution heat exchanger 14, absorber 4 also has weak solution pipeline to be communicated with the second absorber 20 through the 3rd solution pump 21 and the 4th solution heat exchanger 22, the first generator 1 also has refrigerant vapour passage to be communicated with the first condenser 5, the first condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 11, after dividing steam chest 15 to also have refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with the second condenser 6 through the second choke valve 17 again, the second generator 2 also has refrigerant vapour passage to be communicated with the second condenser 6, the 3rd generator 19 also has refrigerant vapour passage to be communicated with the second absorber 20, the second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 10, evaporimeter 7 also has refrigerant vapour passage to be communicated with absorber 4 and absorption-generator 3 respectively, the first generator 1 and the 3rd generator 19 also have respectively the thermal medium of driving pipeline to be communicated with outside, absorption-generator 3 also has heated medium pipeline to be communicated with outside, absorber 4, the first condenser 5 and the second absorber 20 also have respectively heated medium pipeline to be communicated with outside, the second condenser 6 also has cooling medium pipeline to be communicated with outside, evaporimeter 7 medium pipeline that also has surplus heat is communicated with outside.
2. in flow process, the weak solution of the second absorber 20 enters absorption-generator 3 through the 4th solution heat exchanger 22, absorb the refrigerant vapour of flash-pot 7 and respectively heat release in heated medium and the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 is through the first solution pump 8, the 3rd solution heat exchanger 18 and the first solution heat exchanger 13 enter the first generator 1, drive heat medium flow through the first generator 1, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of the first generator 1 enters the 3rd generator 19 through the first solution heat exchanger 13, drive heat medium flow through the 3rd generator 19, the solution that heating enters in it discharges and provides refrigerant vapour to the second absorber 20, the concentrated solution of the 3rd generator 19 absorption-generator 3 of flowing through again after the 3rd solution heat exchanger 18, after heat absorbing part vaporization, enter minute steam chest 15, the refrigerant vapour that divides steam chest 15 to discharge offers the second generator 2 and makes its driving thermal medium, divide the concentrated solution of steam chest 15 to enter the second generator 2 through the second solution heat exchanger 14, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 6, the concentrated solution of the second generator 2 enters absorber 4 through the second solution pump 9 and the second solution heat exchanger 14, absorb the refrigerant vapour of flash-pot 7 heat release in heated medium, the refrigerant vapour heat release of the second generator 2 of flowing through becomes cryogen liquid, through the second choke valve 17 throttlings, enter the second condenser 16 again, the weak solution of absorber 4 enters the second absorber 20 through the 3rd solution pump 21 and the 4th solution heat exchanger 22, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of the first condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 5 enters evaporimeter 7 through choke valve 11 throttlings, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 6 enters evaporimeter 7 through 10 pressurizations of cryogen liquid pump, the cryogen liquid that waste heat MEDIA FLOW enters in it through evaporimeter 7, heating becomes refrigerant vapour and to absorption-generator 3 and absorber 4, provides respectively, forms the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 4 has surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive and is achieved in that
1. in structure, it is mainly comprised of the first generator, the second generator, the 3rd generator, absorption-generator, absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, cryogen liquid pump, choke valve, the second choke valve, the 3rd choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger, the 4th solution heat exchanger, the 5th solution heat exchanger and a minute steam chest, absorber 4 has weak solution pipeline to be communicated with absorption-generator 3 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 22, absorption-generator 3 also has weak solution pipeline through the first solution pump 8, the 3rd solution heat exchanger 18 and the first solution heat exchanger 13 are communicated with the first generator 1, the first generator 1 also has concentrated solution pipeline to be communicated with the 3rd generator 19 through the first solution heat exchanger 13, the 3rd generator 19 also has concentrated solution pipeline to be communicated with a minute steam chest 15 through the 3rd solution heat exchanger 18 and absorption-generator 3, divide steam chest 15 to also have concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 14, the second generator 2 also has concentrated solution pipeline through the second solution pump 9, the second solution heat exchanger 14 and the 4th solution heat exchanger 22 are communicated with absorber 4, absorber 4 also has weak solution pipeline to be communicated with the second absorber 20 through the 3rd solution pump 21 and the 5th solution heat exchanger 24, the first generator 1 also has refrigerant vapour passage to be communicated with the first condenser 5, the first condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 11, after dividing steam chest 15 to also have refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with the second condenser 6 through the 3rd choke valve 23 again, the second generator 2 also has refrigerant vapour passage to be communicated with the second condenser 6, the 3rd generator 19 also has refrigerant vapour passage to be communicated with the second absorber 20, the second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 10, evaporimeter 7 also has cryogen liquid pipeline to be communicated with the second evaporimeter 16 through the second choke valve 17, evaporimeter 7 also has refrigerant vapour passage to be communicated with absorber 4, the second evaporimeter 16 also has refrigerant vapour passage to be communicated with absorption-generator 3, the first generator 1 and the 3rd generator 19 also have respectively the thermal medium of driving pipeline to be communicated with outside, absorption-generator 3 also has heated medium pipeline to be communicated with outside, absorber 4, the first condenser 5 and the second absorber 20 also have respectively heated medium pipeline to be communicated with outside, the second condenser 6 also has cooling medium pipeline to be communicated with outside, evaporimeter 7 and the second evaporimeter 16 medium pipeline that also has surplus heat is respectively communicated with outside.
2. in flow process, the weak solution of the second absorber 20 enters absorption-generator 3 through the 5th solution heat exchanger 24 and the 4th solution heat exchanger 22, absorption from the refrigerant vapour of the second evaporimeter 16 and respectively heat release in heated medium and the solution of the absorption-generator 3 of flowing through, the weak solution of absorption-generator 3 is through the first solution pump 8, the 3rd solution heat exchanger 18 and the first solution heat exchanger 13 enter the first generator 1, drive heat medium flow through the first generator 1, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of the first generator 1 enters the 3rd generator 19 through the first solution heat exchanger 13, drive heat medium flow through the 3rd generator 19, the solution that heating enters in it discharges and provides refrigerant vapour to the second absorber 20, the concentrated solution of the 3rd generator 19 absorption-generator 3 of flowing through again after the 3rd solution heat exchanger 18, after heat absorbing part vaporization, enter minute steam chest 15, the refrigerant vapour that divides steam chest 15 to discharge offers the second generator 2 and makes its driving thermal medium, divide the concentrated solution of steam chest 15 to enter the second generator 2 through the second solution heat exchanger 14, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 6, the concentrated solution of the second generator 2 is through the second solution pump 9, the second solution heat exchanger 14 and the 4th solution heat exchanger 22 enter absorber 4, absorb the refrigerant vapour of flash-pot 7 heat release in heated medium, the refrigerant vapour heat release of the second generator 2 of flowing through becomes cryogen liquid, through the 3rd choke valve 23 throttlings, enter the second condenser 6 again, the weak solution of absorber 4 enters the second absorber 20 through the 3rd solution pump 21 and the 5th solution heat exchanger 24, absorb refrigerant vapour heat release in heated medium, the refrigerant vapour heat release of the first condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 5 enters evaporimeter 7 through choke valve 11 throttlings, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 6 enters evaporimeter 7 through 10 pressurizations of cryogen liquid pump, the cryogen liquid of evaporimeter 7 is divided into two-way---and the first via absorbs waste heat and becomes refrigerant vapour and provide to absorber 4, second tunnel the second choke valve 17 throttlings enter the second evaporimeter 16, absorbing waste heat becomes refrigerant vapour and provides to absorption-generator 3, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 5 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, it is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump, the first solution heat exchanger, the second solution heat exchanger, solution choke valve and a minute steam chest, absorber 4 has weak solution pipeline to be communicated with a minute steam chest 15 through solution choke valve 25 and absorption-generator 3, divide steam chest 15 to also have concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 14, the second generator 2 also has concentrated solution pipeline to be communicated with absorber 4 through the second solution pump 9 and the second solution heat exchanger 14, absorption-generator 3 also has weak solution pipeline to be communicated with the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, the first generator 1 also has concentrated solution pipeline to be communicated with absorption-generator 3 through the first solution heat exchanger 13, the first generator 1 also has refrigerant vapour passage to be communicated with the first condenser 5, the first condenser 5 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through choke valve 11, after dividing steam chest 15 to also have refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 7 through the second cryogen liquid pump 12 again, the second generator 2 also has refrigerant vapour passage to be communicated with the second condenser 6, the second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 10, evaporimeter 7 also has refrigerant vapour passage to be communicated with absorber 4 and absorption-generator 3 respectively, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorption-generator 3 also has heated medium pipeline to be communicated with outside, absorber 4 and the first condenser 5 also have respectively heated medium pipeline to be communicated with outside, the second condenser 6 also has cooling medium pipeline to be communicated with outside, evaporimeter 7 medium pipeline that also has surplus heat is communicated with outside.
2. in flow process, the weak solution of the absorber 4 absorption-generator 3 of flowing through after solution choke valve 25, after heat absorbing part vaporization, enter minute steam chest 15, the refrigerant vapour that divides steam chest 15 to discharge offers the second generator 2 and makes its driving thermal medium, divide the concentrated solution of steam chest 15 to enter the second generator 2 through the second solution heat exchanger 14, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 6, the concentrated solution of the second generator 2 enters absorber 4 through the second solution pump 9 and the second solution heat exchanger 14, absorb the refrigerant vapour of flash-pot 7 heat release in heated medium, the refrigerant vapour heat release of the second generator 2 of flowing through becomes cryogen liquid, through the second cryogen liquid pump 12 pressurizations, enter evaporimeter 7 again, the weak solution of absorption-generator 3 enters the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, the solution that drives heat medium flow to enter in it through the first generator 1, heating discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of the first generator 1 through the first solution heat exchanger 13 enter absorptions-generator 3, the refrigerant vapour that absorbs flash-pot 7 also respectively heat release in heated medium and the solution of the absorption-generator 3 of flowing through, the refrigerant vapour heat release of the first condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 5 enters evaporimeter 7 through choke valve 11 throttlings, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 6 enters evaporimeter 7 through 10 pressurizations of cryogen liquid pump, the cryogen liquid that waste heat MEDIA FLOW enters in it through evaporimeter 7, heating becomes refrigerant vapour and to absorption-generator 3 and absorber 4, provides respectively, forms the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 6 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, it is mainly comprised of the first generator, the second generator, absorption-generator, absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and a minute steam chest, absorber 4 has weak solution pipeline to be communicated with a minute steam chest 15 through the 3rd solution heat exchanger 18 and absorption-generator 3, divide steam chest 15 to also have concentrated solution pipeline to be communicated with the second generator 2 through the second solution heat exchanger 14, the second generator 2 also has concentrated solution pipeline through the second solution pump 9, the second solution heat exchanger 14 and the 3rd solution heat exchanger 18 are communicated with absorber 4, absorption-generator 3 also has weak solution pipeline to be communicated with the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, the first generator 1 also has concentrated solution pipeline to be communicated with absorption-generator 3 through the first solution heat exchanger 13, the first generator 1 also has refrigerant vapour passage to be communicated with the first condenser 5, the first condenser 5 also has cryogen liquid pipeline to be communicated with the second evaporimeter 16 through choke valve 11, the second evaporimeter 16 also has refrigerant vapour passage to be communicated with absorption-generator 3, after dividing steam chest 15 to also have refrigerant vapour passage to be communicated with the second generator 2, the second generator 2 has cryogen liquid pipeline to be communicated with evaporimeter 7 through the second cryogen liquid pump 12 again, the second generator 2 also has refrigerant vapour passage to be communicated with the second condenser 6, the second condenser 6 also has cryogen liquid pipeline to be communicated with evaporimeter 7 through cryogen liquid pump 10, evaporimeter 7 also has refrigerant vapour passage to be communicated with absorber 4, the first generator 1 drives thermal medium pipeline to be communicated with outside in addition, absorption-generator 3 also has heated medium pipeline to be communicated with outside, absorber 4 and the first condenser 5 also have respectively heated medium pipeline to be communicated with outside, the second condenser 6 also has cooling medium pipeline to be communicated with outside, evaporimeter 7 and the second evaporimeter 16 medium pipeline that also has surplus heat is respectively communicated with outside.
2. in flow process, the weak solution of the absorber 4 absorption-generator 3 of flowing through after the 3rd solution heat exchanger 18, after heat absorbing part vaporization, enter minute steam chest 15, the refrigerant vapour that divides steam chest 15 to discharge offers the second generator 2 and makes its driving thermal medium, divide the concentrated solution of steam chest 15 to enter the second generator 2 through the second solution heat exchanger 14, refrigerant vapour second generator 2 of flowing through, the solution that heating enters in it discharges and provides refrigerant vapour to the second condenser 6, the concentrated solution of the second generator 2 is through the second solution pump 9, the second solution heat exchanger 14 and the 3rd solution heat exchanger 18 enter absorber 4, absorb the refrigerant vapour of flash-pot 7 heat release in heated medium, the refrigerant vapour heat release of the second generator 2 of flowing through becomes cryogen liquid, through the second cryogen liquid pump 12 pressurizations, enter evaporimeter 7 again, the weak solution of absorption-generator 3 enters the first generator 1 through the first solution pump 8 and the first solution heat exchanger 13, the solution that drives heat medium flow to enter in it through the first generator 1, heating discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of the first generator 1 through the first solution heat exchanger 13 enter absorptions-generator 3, absorb from the refrigerant vapour of the second evaporimeter 16 also respectively heat release in heated medium and the solution of the absorption-generator 3 of flowing through, the refrigerant vapour heat release of the first condenser 5 becomes cryogen liquid in heated medium, the cryogen liquid of the first condenser 5 enters the second evaporimeter 16 through choke valve 11 throttlings, waste heat MEDIA FLOW is through the second evaporimeter 16, the cryogen liquid that heating enters in it becomes refrigerant vapour and provides to absorption-generator 3, the refrigerant vapour heat release of the second condenser 6 becomes cryogen liquid in cooling medium, the cryogen liquid of the second condenser 6 enters evaporimeter 7 through 10 pressurizations of cryogen liquid pump, waste heat MEDIA FLOW is through evaporimeter 7, the cryogen liquid that heating enters in it becomes refrigerant vapour and provides to absorber 4, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 7 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, at the band shown in Fig. 5, have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, increase by the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, there is weak solution pipeline to be communicated with the first generator 1 and to be adjusted into absorption-generator 3 and to have weak solution pipeline to be communicated with the second absorber 20 through the first solution pump 8 and the 3rd solution heat exchanger 18 through the first solution pump 8 and the first solution heat exchanger 13 in absorption-generator 3, the second absorber 20 has weak solution pipeline to be communicated with the first generator 1 through the 3rd solution pump 21 and the first solution heat exchanger 13 again, the first generator 1 is had concentrated solution pipeline to be communicated with absorption-generator 3 through the first solution heat exchanger 13 to be adjusted into the first generator 1 has concentrated solution pipeline to be communicated with the 3rd generator 19 through the first solution heat exchanger 13, the 3rd generator 19 has concentrated solution pipeline to be communicated with absorption-generator 3 through the 3rd solution heat exchanger 18 again, the 3rd generator 19 also has refrigerant vapour passage to be communicated with the second absorber 20, the 3rd generator 19 drives thermal medium pipeline to be communicated with outside in addition, the second absorber 20 also has heated medium pipeline to be communicated with outside.
2. in flow process, the weak solution of absorption-generator 3 enters the second absorber 20 through the first solution pump 8 and the 3rd solution heat exchanger 18, absorption from the refrigerant vapour of the 3rd generator 19 heat release in heated medium, the weak solution of the second absorber 20 enters the first generator 1 through the 3rd solution pump 21 and the first solution heat exchanger 13, the concentrated solution of the first generator 1 enters the 3rd generator 19 through the first solution heat exchanger 13, drive heat medium flow through the 3rd generator 19, the solution that heating enters in it discharges and provides refrigerant vapour to the second absorber 20, the concentrated solution of the 3rd generator 19 enters absorption-generator 3 through the 3rd solution heat exchanger 18, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 8 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, at the band shown in Fig. 1, have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first solution pump 8 is set up weak solution pipeline and is communicated with newly-increased generator A through newly-increased solution heat exchanger C, newly-increased generator A also has concentrated solution pipeline to be communicated with a minute steam chest 15 through newly-increased solution heat exchanger C and absorption-generator 3, after having refrigerant vapour passage to be communicated with the first condenser 5 to be adjusted into the first generator 1 to have refrigerant vapour passage to be communicated with newly-increased generator A in the first generator 1, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 5.
2. in flow process, the refrigerant vapour that the first generator 1 produces is as the driving thermal medium of newly-increased generator A, the part weak solution of absorption-generator 3 enters newly-increased generator A through the first solution pump 8 and newly-increased solution heat exchanger C, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of newly-increased generator A enters minute steam chest 15 through newly-increased solution heat exchanger C and absorption-generator 3, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, through newly-increased choke valve B throttling, enter the first condenser 5 again, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Fig. 9 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, at the band shown in Fig. 1, have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with the first generator 1 and to be adjusted into absorption-generator 3 and to have weak solution pipeline through the first solution pump 8 through the first solution pump 8 and the first solution heat exchanger 13 in absorption-generator 3, the first solution heat exchanger 13 and newly-increased solution heat exchanger C are communicated with the first generator 1, the first generator 1 is had concentrated solution pipeline to be communicated with a minute steam chest 15 through the first solution heat exchanger 13 and absorption-generator 3 to be adjusted into the first generator 1 has concentrated solution pipeline to be communicated with newly-increased generator A through increasing solution heat exchanger C newly, newly-increased generator A has concentrated solution pipeline to be communicated with a minute steam chest 15 through the first solution heat exchanger 13 and absorption-generator 3 again, after having refrigerant vapour passage to be communicated with the first condenser 5 to be adjusted into the first generator 1 to have refrigerant vapour passage to be communicated with newly-increased generator A in the first generator 1, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 5.
2. in flow process, the refrigerant vapour that the first generator 1 produces is as the driving thermal medium of newly-increased generator A, the weak solution of absorption-generator 3 is through the first solution pump 8, the first solution heat exchanger 13 and newly-increased solution heat exchanger C enter the first generator 1, the concentrated solution of the first generator 1 enters newly-increased generator A through newly-increased solution heat exchanger C, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of newly-increased generator A enters minute steam chest 15 through the first solution heat exchanger 13 and absorption-generator 3, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, through newly-increased choke valve B throttling, enter the first condenser 5 again, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Figure 10 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, at the band shown in Fig. 1, have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the first generator 1 and to be adjusted into absorption-generator 3 and to have weak solution pipeline to be communicated with newly-increased generator A through the first solution pump 8 and the first solution heat exchanger 13 through the first solution pump 8 and the first solution heat exchanger 13 in absorption-generator 3, newly-increased generator A has concentrated solution pipeline to be communicated with the first generator 1 through newly-increased solution pump D and newly-increased solution heat exchanger C again, the first generator 1 there is is concentrated solution pipeline to be communicated with a minute steam chest 15 through the first solution heat exchanger 13 and absorption-generator 3 to be adjusted into the first generator 1 and have concentrated solution pipeline through increasing solution heat exchanger C newly, the first solution heat exchanger 13 and absorption-generator 3 are communicated with a minute steam chest 15, after having refrigerant vapour passage to be communicated with the first condenser 5 to be adjusted into the first generator 1 to have refrigerant vapour passage to be communicated with newly-increased generator A in the first generator 1, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 5.
2. in flow process, the refrigerant vapour that the first generator 1 produces is as the driving thermal medium of newly-increased generator A, the weak solution of absorption-generator 3 enters newly-increased generator A through the first solution pump 8 and the first solution heat exchanger 13, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of newly-increased generator A enters the first generator 1 through newly-increased solution pump D and newly-increased solution heat exchanger C, the concentrated solution of the first generator 1 is through newly-increased solution heat exchanger C, the first solution heat exchanger 13 and absorption-generator 3 enter minute steam chest 15, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, through newly-increased choke valve B throttling, enter the first condenser 5 again, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Figure 11 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
1. in structure, at the band shown in Fig. 3, have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, cancel absorption-generator 3 and the outside heated medium pipeline being communicated with, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, absorption-generator 3 is had to weak solution pipeline through the first solution pump 8, the 3rd solution heat exchanger 18 and the first solution heat exchanger 13 are communicated with the first generator 1 and are adjusted into absorption-generator 3 and have weak solution pipeline through the first solution pump 8, the 3rd solution heat exchanger 18, the first solution heat exchanger 13 and newly-increased solution heat exchanger C are communicated with the first generator 1, there is concentrated solution pipeline to be communicated with the 3rd generator 19 through the first solution heat exchanger 13 to be adjusted into the first generator 1 to have concentrated solution pipeline to be communicated with newly-increased generator A through newly-increased solution heat exchanger C in the first generator 1, newly-increased generator A has concentrated solution pipeline to be communicated with the 3rd generator 19 through the first solution heat exchanger 13 again, after having refrigerant vapour passage to be communicated with the first condenser 5 to be adjusted into the first generator 1 to have refrigerant vapour passage to be communicated with newly-increased generator A in the first generator 1, newly-increased generator A has cryogen liquid pipeline to be communicated with the first condenser 5 through newly-increased choke valve B again, newly-increased generator A also has refrigerant vapour passage to be communicated with the first condenser 5.
2. in flow process, the refrigerant vapour that the first generator 1 produces is as the driving thermal medium of newly-increased generator A, the weak solution of absorption-generator 3 is through the first solution pump 8, the 3rd solution heat exchanger 18, the first solution heat exchanger 13 and newly-increased solution heat exchanger C enter the first generator 1, the concentrated solution of the first generator 1 enters newly-increased generator A through newly-increased solution heat exchanger C, refrigerant vapour is flowed through and is increased generator A newly, the solution that heating enters in it discharges and provides refrigerant vapour to the first condenser 5, the concentrated solution of newly-increased generator A enters the 3rd generator 19 through the first solution heat exchanger 13, the refrigerant vapour heat release of newly-increased generator A of flowing through becomes cryogen liquid, through newly-increased choke valve B throttling, enter the first condenser 5 again, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
Band shown in Figure 12 the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat is achieved in that
At the band shown in Figure 11, have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, cancel the 3rd generator and the outside driving thermal medium pipeline being communicated with, increase newly-increased the second choke valve, the first generator 1 set up refrigerant vapour passage and be communicated with the 3rd generator 19 after the 3rd generator 19 have again cryogen liquid pipeline warp to increase the second choke valve E newly to be communicated with the first condenser 5; The first generator provides refrigerant vapour to do it to the 3rd generator and drives thermal medium, the refrigerant vapour solution that the 3rd generator 19, heating enter in it of flowing through discharges and provides refrigerant vapour to the second absorber 20, the refrigerant vapour heat release of the 3rd generator 19 of flowing through becomes cryogen liquid, through newly-increased the second choke valve E throttling, enters the first condenser 5 again, forms band the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat.
The effect that the technology of the present invention can realize---band proposed by the invention the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat, has following effect and advantage:
(1) band proposing the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat, flow process is reasonable, can improve the utilization rate to residual heat resources.
(2) band proposing the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat, the thermic load of its absorptions-generator is adjustable, correspondingly obtains the adjustable double-effect process of thermic load, thereby under the certain performance index prerequisite of maintenance, realizes the adjusting of heat supply temperature.
(3) band proposing the 3rd class absorption heat pump that economic benefits and social benefits drive that has surplus heat, has further enriched absorption heat pump kind and flow process, can realize better mutual coupling the between heat pump heat supply and user's request.
(4) utilize band of the present invention to have surplus heat the 3rd class absorption heat pump that economic benefits and social benefits drive, can expand the temperature operation interval of absorption heat pump, has expanded and enriched the range of application of absorption heat pump, has good creativeness, novelty and practicality.

Claims (21)

1. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, absorption-generator, the second generator, absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger and a minute steam chest; absorber (4) has weak solution pipeline to be communicated with absorption-generator (3), absorption-generator (3) also has weak solution pipeline to be communicated with the first generator (1) through the first solution pump (8) and the first solution heat exchanger (13), the first generator (1) also has concentrated solution pipeline to be communicated with a minute steam chest (15) through the first solution heat exchanger (13) and absorption-generator (3), divide steam chest (15) to also have concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (14), the second generator (2) also has concentrated solution pipeline to be communicated with absorber (4) through the second solution pump (9) and the second solution heat exchanger (14), the first generator (1) also has refrigerant vapour passage to be communicated with the first condenser (5), the first condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (11), after dividing steam chest (15) to also have refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline through the second cryogen liquid pump (12), be communicated with evaporimeter (7) or be communicated with the second condenser (6) through the second choke valve (17) again, the second generator (2) also has refrigerant vapour passage to be communicated with the second condenser (6), the second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (10), evaporimeter (7) also has refrigerant vapour passage to be communicated with absorber (4) and absorption-generator (3) respectively, the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorption-generator (3) or in addition heated medium pipeline are communicated with outside, absorber (4) and the first condenser (5) also have respectively heated medium pipeline to be communicated with outside, the second condenser (6) also has cooling medium pipeline to be communicated with outside, evaporimeter (7) medium pipeline that also has surplus heat is communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
2. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, absorption-generator, the second generator, absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second choke valve, the second cryogen liquid pump or the 3rd choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and a minute steam chest; absorber (4) has weak solution pipeline to be communicated with absorption-generator (3) through the 3rd solution heat exchanger (18), absorption-generator (3) also has weak solution pipeline to be communicated with the first generator (1) through the first solution pump (8) and the first solution heat exchanger (13), the first generator (1) also has concentrated solution pipeline to be communicated with a minute steam chest (15) through the first solution heat exchanger (13) and absorption-generator (3), divide steam chest (15) to also have concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (14), the second generator (2) also has concentrated solution pipeline through the second solution pump (9), the second solution heat exchanger (14) and the 3rd solution heat exchanger (18) are communicated with absorber (4), the first generator (1) also has refrigerant vapour passage to be communicated with the first condenser (5), the first condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (11), after dividing steam chest (15) to also have refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline through the second cryogen liquid pump (12), be communicated with evaporimeter (7) or be communicated with the second condenser (6) through the 3rd choke valve (23) again, the second generator (2) also has refrigerant vapour passage to be communicated with the second condenser (6), the second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (10), evaporimeter (7) also has cryogen liquid pipeline to be communicated with the second evaporimeter (16) through the second choke valve (17), evaporimeter (7) also has refrigerant vapour passage to be communicated with absorber (4), the second evaporimeter (16) also has refrigerant vapour passage to be communicated with absorption-generator (3), the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorption-generator (3) or in addition heated medium pipeline are communicated with outside, absorber (4) and the first condenser (5) also have respectively heated medium pipeline to be communicated with outside, the second condenser (6) also has cooling medium pipeline to be communicated with outside, evaporimeter (7) and the second evaporimeter (16) medium pipeline that also has surplus heat is respectively communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
3. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, the second generator, the 3rd generator, absorption-generator, absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger, the 4th solution heat exchanger and a minute steam chest; absorber (4) has weak solution pipeline to be communicated with absorption-generator (3) through the 4th solution heat exchanger (22), absorption-generator (3) also has weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18) and the first solution heat exchanger (13) are communicated with the first generator (1), the first generator (1) also has concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13), the 3rd generator (19) also has concentrated solution pipeline to be communicated with a minute steam chest (15) through the 3rd solution heat exchanger (18) and absorption-generator (3), divide steam chest (15) to also have concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (14), the second generator (2) also has concentrated solution pipeline to be communicated with absorber (4) through the second solution pump (9) and the second solution heat exchanger (14), absorber (4) also has weak solution pipeline to be communicated with the second absorber (20) through the 3rd solution pump (21) and the 4th solution heat exchanger (22), the first generator (1) also has refrigerant vapour passage to be communicated with the first condenser (5), the first condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (11), after dividing steam chest (15) to also have refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline through the second cryogen liquid pump (12), be communicated with evaporimeter (7) or be communicated with the second condenser (6) through the second choke valve (17) again, the second generator (2) also has refrigerant vapour passage to be communicated with the second condenser (6), the 3rd generator (19) also has refrigerant vapour passage to be communicated with the second absorber (20), the second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (10), evaporimeter (7) also has refrigerant vapour passage to be communicated with absorber (4) and absorption-generator (3) respectively, the first generator (1) and the 3rd generator (19) also have respectively the thermal medium of driving pipeline to be communicated with outside, absorption-generator (3) or in addition heated medium pipeline are communicated with outside, absorber (4), the first condenser (5) and the second absorber (20) also have respectively heated medium pipeline to be communicated with outside, the second condenser (6) also has cooling medium pipeline to be communicated with outside, evaporimeter (7) medium pipeline that also has surplus heat is communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
4. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, mainly by the first generator, the second generator, the 3rd generator, absorption-generator, absorber, the second absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, the 3rd solution pump, cryogen liquid pump, choke valve, the second choke valve, the second cryogen liquid pump or the 3rd choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger, the 4th solution heat exchanger, the 5th solution heat exchanger and a minute steam chest form, absorber (4) has weak solution pipeline to be communicated with absorption-generator (3) through the 5th solution heat exchanger (24) and the 4th solution heat exchanger (22), absorption-generator (3) also has weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18) and the first solution heat exchanger (13) are communicated with the first generator (1), the first generator (1) also has concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13), the 3rd generator (19) also has concentrated solution pipeline to be communicated with a minute steam chest (15) through the 3rd solution heat exchanger (18) and absorption-generator (3), divide steam chest (15) to also have concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (14), the second generator (2) also has concentrated solution pipeline through the second solution pump (9), the second solution heat exchanger (14) and the 4th solution heat exchanger (22) are communicated with absorber (4), absorber (4) also has weak solution pipeline to be communicated with the second absorber (20) through the 3rd solution pump (21) and the 5th solution heat exchanger (24), the first generator (1) also has refrigerant vapour passage to be communicated with the first condenser (5), the first condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (11), after dividing steam chest (15) to also have refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline through the second cryogen liquid pump (12), be communicated with evaporimeter (7) or be communicated with the second condenser (6) through the 3rd choke valve (23) again, the second generator (2) also has refrigerant vapour passage to be communicated with the second condenser (6), the 3rd generator (19) also has refrigerant vapour passage to be communicated with the second absorber (20), the second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (10), evaporimeter (7) also has cryogen liquid pipeline to be communicated with the second evaporimeter (16) through the second choke valve (17), evaporimeter (7) also has refrigerant vapour passage to be communicated with absorber (4), the second evaporimeter (16) also has refrigerant vapour passage to be communicated with absorption-generator (3), the first generator (1) and the 3rd generator (19) also have respectively the thermal medium of driving pipeline to be communicated with outside, absorption-generator (3) or in addition heated medium pipeline are communicated with outside, absorber (4), the first condenser (5) and the second absorber (20) also have respectively heated medium pipeline to be communicated with outside, the second condenser (6) also has cooling medium pipeline to be communicated with outside, evaporimeter (7) and the second evaporimeter (16) medium pipeline that also has surplus heat is respectively communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
5. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, absorption-generator, the second generator, absorber, the first condenser, the second condenser, evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger, solution choke valve and a minute steam chest; absorber (4) has weak solution pipeline to be communicated with a minute steam chest (15) through solution choke valve (25) and absorption-generator (3), divide steam chest (15) to also have concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (14), the second generator (2) also has concentrated solution pipeline to be communicated with absorber (4) through the second solution pump (9) and the second solution heat exchanger (14), absorption-generator (3) also has weak solution pipeline to be communicated with the first generator (1) through the first solution pump (8) and the first solution heat exchanger (13), the first generator (1) also has concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13), the first generator (1) also has refrigerant vapour passage to be communicated with the first condenser (5), the first condenser (5) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through choke valve (11), after dividing steam chest (15) to also have refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline through the second cryogen liquid pump (12), be communicated with evaporimeter (7) or be communicated with the second condenser (6) through the second choke valve (17) again, the second generator (2) also has refrigerant vapour passage to be communicated with the second condenser (6), the second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (10), evaporimeter (7) also has refrigerant vapour passage to be communicated with absorber (4) and absorption-generator (3) respectively, the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorption-generator (3) or in addition heated medium pipeline are communicated with outside, absorber (4) and the first condenser (5) also have respectively heated medium pipeline to be communicated with outside, the second condenser (6) also has cooling medium pipeline to be communicated with outside, evaporimeter (7) medium pipeline that also has surplus heat is communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
6. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, is mainly comprised of the first generator, absorption-generator, the second generator, absorber, the first condenser, the second condenser, evaporimeter, the second evaporimeter, the first solution pump, the second solution pump, cryogen liquid pump, choke valve, the second cryogen liquid pump or the second choke valve, the first solution heat exchanger, the second solution heat exchanger, the 3rd solution heat exchanger and a minute steam chest; absorber (4) has weak solution pipeline to be communicated with a minute steam chest (15) through the 3rd solution heat exchanger (18) and absorption-generator (3), divide steam chest (15) to also have concentrated solution pipeline to be communicated with the second generator (2) through the second solution heat exchanger (14), the second generator (2) also has concentrated solution pipeline through the second solution pump (9), the second solution heat exchanger (14) and the 3rd solution heat exchanger (18) are communicated with absorber (4), absorption-generator (3) also has weak solution pipeline to be communicated with the first generator (1) through the first solution pump (8) and the first solution heat exchanger (13), the first generator (1) also has concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13), the first generator (1) also has refrigerant vapour passage to be communicated with the first condenser (5), the first condenser (5) also has cryogen liquid pipeline to be communicated with the second evaporimeter (16) through choke valve (11), the second evaporimeter (16) also has refrigerant vapour passage to be communicated with absorption-generator (3), after dividing steam chest (15) to also have refrigerant vapour passage to be communicated with the second generator (2), the second generator (2) has cryogen liquid pipeline through the second cryogen liquid pump (12), be communicated with evaporimeter (7) or be communicated with the second condenser (6) through the second choke valve (17) again, the second generator (2) also has refrigerant vapour passage to be communicated with the second condenser (6), the second condenser (6) also has cryogen liquid pipeline to be communicated with evaporimeter (7) through cryogen liquid pump (10), evaporimeter (7) also has refrigerant vapour passage to be communicated with absorber (4), the first generator (1) drives thermal medium pipeline to be communicated with outside in addition, absorption-generator (3) or in addition heated medium pipeline are communicated with outside, absorber (4) and the first condenser (5) also have respectively heated medium pipeline to be communicated with outside, the second condenser (6) also has cooling medium pipeline to be communicated with outside, evaporimeter (7) and the second evaporimeter (16) medium pipeline that also has surplus heat is respectively communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
7. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at band claimed in claim 5, increase by the 3rd generator, the second absorber, the 3rd solution pump and the 3rd solution heat exchanger, to absorb-generator (3) has weak solution pipeline to be communicated with the first generator (1) and to be adjusted into absorption-generator (3) and to have weak solution pipeline to be communicated with the second absorber (20) through the first solution pump (8) and the 3rd solution heat exchanger (18) through the first solution pump (8) and the first solution heat exchanger (13), the second absorber (20) has weak solution pipeline to be communicated with the first generator (1) through the 3rd solution pump (21) and the first solution heat exchanger (13) again, the first generator (1) is had concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13) to be adjusted into the first generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13), the 3rd generator (19) has concentrated solution pipeline to be communicated with absorption-generator (3) through the 3rd solution heat exchanger (18) again, the 3rd generator (19) also has refrigerant vapour passage to be communicated with the second absorber (20), the 3rd generator (19) drives thermal medium pipeline to be communicated with outside in addition, the second absorber (20) also has heated medium pipeline to be communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
8. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at band claimed in claim 6, increase by the 3rd generator, the second absorber, the 3rd solution pump and the 4th solution heat exchanger, to absorb-generator (3) has weak solution pipeline to be communicated with the first generator (1) and to be adjusted into absorption-generator (3) and to have weak solution pipeline to be communicated with the second absorber (20) through the first solution pump (8) and the 4th solution heat exchanger (22) through the first solution pump (8) and the first solution heat exchanger (13), the second absorber (20) has weak solution pipeline to be communicated with the first generator (1) through the 3rd solution pump (21) and the first solution heat exchanger (13) again, the first generator (1) is had concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13) to be adjusted into the first generator (1) has concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13), the 3rd generator (19) has concentrated solution pipeline to be communicated with absorption-generator (3) through the 4th solution heat exchanger (22) again, the 3rd generator (19) also has refrigerant vapour passage to be communicated with the second absorber (20), the 3rd generator (19) drives thermal medium pipeline to be communicated with outside in addition, the second absorber (20) also has heated medium pipeline to be communicated with outside, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
9. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 1-2, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first solution pump (8) is set up weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with a minute steam chest (15) through newly-increased solution heat exchanger (C) and absorption-generator (3), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
10. the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 1-2, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, to absorb-generator (3) has weak solution pipeline to be communicated with the first generator (1) and to be adjusted into absorption-generator (3) and to have weak solution pipeline through the first solution pump (8) through the first solution pump (8) and the first solution heat exchanger (13), the first solution heat exchanger (13) and newly-increased solution heat exchanger (C) are communicated with the first generator (1), the first generator (1) is had concentrated solution pipeline to be communicated with a minute steam chest (15) through the first solution heat exchanger (13) and absorption-generator (3) to be adjusted into the first generator (1) has concentrated solution pipeline to be communicated with newly-increased generator (A) through increasing solution heat exchanger (C) newly, newly-increased generator (A) has concentrated solution pipeline to be communicated with a minute steam chest (15) through the first solution heat exchanger (13) and absorption-generator (3) again, after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
11. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 1-2, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator (3) has weak solution pipeline to be communicated with the first generator (1) and to be adjusted into absorption-generator (3) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the first solution pump (8) and the first solution heat exchanger (13) through the first solution pump (8) and the first solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the first generator (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C) again, the first generator (1) there is is concentrated solution pipeline to be communicated with a minute steam chest (15) through the first solution heat exchanger (13) and absorption-generator (3) to be adjusted into the first generator (1) and have concentrated solution pipeline through increasing solution heat exchanger (C) newly, the first solution heat exchanger (13) and absorption-generator (3) are communicated with a minute steam chest (15), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
12. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 3-4, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, to absorb-generator (3) and have weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18) and the first solution heat exchanger (13) are communicated with the first generator (1) and are adjusted into absorption-generator (3) and have weak solution pipeline through the first solution heat exchanger (13), to be communicated with the first generator (1) connected sum through increasing solution heat exchanger (C) newly with newly-increased generator (A) more respectively afterwards through the first solution pump (8) and the 3rd solution heat exchanger (18) again, newly-increased generator (A) also has concentrated solution pipeline to be communicated with the 3rd generator (19) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
13. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 3-4, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, to absorb-generator (3) and have weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18) and the first solution heat exchanger (13) are communicated with the first generator (1) and are adjusted into absorption-generator (3) and have weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18), the first solution heat exchanger (13) and newly-increased solution heat exchanger (C) are communicated with the first generator (1), there is concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C) in the first generator (1), newly-increased generator (A) has concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13) again, after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
14. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 3-4, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator (3) and have weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18) and the first solution heat exchanger (13) are communicated with the first generator (1) and are adjusted into absorption-generator (3) and have weak solution pipeline through the first solution pump (8), the 3rd solution heat exchanger (18) and the first solution heat exchanger (13) are communicated with newly-increased generator (A), newly-increased generator (A) has concentrated solution pipeline to be communicated with the first generator (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C) again, there is concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with the 3rd generator (19) through newly-increased solution heat exchanger (C) and the first solution heat exchanger (13) in the first generator (1), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
15. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 5-6, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the first solution pump (8) is set up weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
16. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 5-6, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, to absorb-generator (3) has weak solution pipeline to be communicated with the first generator (1) and to be adjusted into absorption-generator (3) and to have weak solution pipeline through the first solution pump (8) through the first solution pump (8) and the first solution heat exchanger (13), the first solution heat exchanger (13) and newly-increased solution heat exchanger (C) are communicated with the first generator (1), there is concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C) in the first generator (1), newly-increased generator (A) has concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13) again, after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
17. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 5-6, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, to absorb-generator (3) has weak solution pipeline to be communicated with the first generator (1) and to be adjusted into absorption-generator (3) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the first solution pump (8) and the first solution heat exchanger (13) through the first solution pump (8) and the first solution heat exchanger (13), newly-increased generator (A) has concentrated solution pipeline to be communicated with the first generator (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C) again, there is concentrated solution pipeline to be communicated with absorption-generator (3) through the first solution heat exchanger (13) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with absorption-generator (3) through newly-increased solution heat exchanger (C) and the first solution heat exchanger (13) in the first generator (1), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
18. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 7-8, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, the 3rd solution pump (21) is set up weak solution pipeline and is communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C), newly-increased generator (A) also has concentrated solution pipeline to be communicated with the 3rd generator (19) through newly-increased solution heat exchanger (C), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
19. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 7-8, increase newly-increased generator, newly-increased choke valve and newly-increased solution heat exchanger, there is weak solution pipeline to be communicated with the first generator (1) and to be adjusted into the second absorber (20) and to have weak solution pipeline through the 3rd solution pump (21) through the 3rd solution pump (21) and the first solution heat exchanger (13) the second absorber (20), the first solution heat exchanger (13) and newly-increased solution heat exchanger (C) are communicated with the first generator (1), there is concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with newly-increased generator (A) through newly-increased solution heat exchanger (C) in the first generator (1), newly-increased generator (A) has concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13) again, after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
20. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, to have surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive at the arbitrary band described in claim 7-8, increase newly-increased generator, newly-increased choke valve, newly-increased solution heat exchanger and newly-increased solution pump, there is weak solution pipeline to be communicated with the first generator (1) and to be adjusted into the second absorber (20) and to have weak solution pipeline to be communicated with newly-increased generator (A) through the 3rd solution pump (21) and the first solution heat exchanger (13) through the 3rd solution pump (21) and the first solution heat exchanger (13) the second absorber (20), newly-increased generator (A) has concentrated solution pipeline to be communicated with the first generator (1) through newly-increased solution pump (D) and newly-increased solution heat exchanger (C) again, there is concentrated solution pipeline to be communicated with the 3rd generator (19) through the first solution heat exchanger (13) to be adjusted into the first generator (1) to have concentrated solution pipeline to be communicated with the 3rd generator (19) through newly-increased solution heat exchanger (C) and the first solution heat exchanger (13) in the first generator (1), after having refrigerant vapour passage to be communicated with the first condenser (5) to be adjusted into the first generator (1) to have refrigerant vapour passage to be communicated with newly-increased generator (A) in the first generator (1), newly-increased generator (A) has cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased choke valve (B) again, newly-increased generator (A) also has refrigerant vapour passage to be communicated with the first condenser (5), form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
21. the 3rd class absorption heat pumps of being with the economic benefits and social benefits that have surplus heat to drive, at claim 12-14, arbitrary band described in 18-20 has surplus heat in the 3rd class absorption heat pump that economic benefits and social benefits drive, cancel the 3rd generator and the outside driving thermal medium pipeline being communicated with, increase newly-increased the second choke valve, the first generator (1) set up refrigerant vapour passage and be communicated with the 3rd generator (19) after the 3rd generator (19) have again cryogen liquid pipeline to be communicated with the first condenser (5) through newly-increased the second choke valve (E)---the first generator provides refrigerant vapour to make its driving thermal medium to the 3rd generator, form the 3rd class absorption heat pump of being with the economic benefits and social benefits that have surplus heat to drive.
CN201210059126.7A 2012-02-27 2012-02-27 Third type absorption heat pump with afterheat double-effect driving function Active CN102607209B (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101458006A (en) * 2009-01-01 2009-06-17 李华玉 Method for enhancing first kind absorption heat pump heat supply temperature and high temperature heat pump
CN101694332A (en) * 2009-09-28 2010-04-14 李华玉 Back-heating type triple-effect first category absorption heat pump
CN101825370A (en) * 2009-09-19 2010-09-08 李华玉 Backheating type double-effect and multi-effect second-class absorption heat pump
CN102116538A (en) * 2011-03-06 2011-07-06 李华玉 Double-effect and triple-effect first-type absorption heat pump with heat return end and heat supply end

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101458006A (en) * 2009-01-01 2009-06-17 李华玉 Method for enhancing first kind absorption heat pump heat supply temperature and high temperature heat pump
CN101825370A (en) * 2009-09-19 2010-09-08 李华玉 Backheating type double-effect and multi-effect second-class absorption heat pump
CN101694332A (en) * 2009-09-28 2010-04-14 李华玉 Back-heating type triple-effect first category absorption heat pump
CN102116538A (en) * 2011-03-06 2011-07-06 李华玉 Double-effect and triple-effect first-type absorption heat pump with heat return end and heat supply end

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