CN101666564B

CN101666564B - Multiple compound first class absorption heat pump

Info

Publication number: CN101666564B
Application number: CN2009101719675A
Authority: CN
Inventors: 李华玉
Original assignee: Individual
Current assignee: Individual
Priority date: 2008-09-17
Filing date: 2009-09-17
Publication date: 2012-01-11
Anticipated expiration: 2029-09-17
Also published as: CN101666564A; CN101363666A

Abstract

The invention relates to a multiple compound first class absorption heat pump, belonging to the technical field of heat pump/refrigeration. A condenser, a throttle, an absorber, an absorption vaporizer, a refrigerant liquid pump or a second throttle are added in a double effect absorption heat pump which is composed of a plurality of generators, a condenser, a vaporizer, an absorber, a throttle, a solution pump and a solution heat exchanger; the newly added condenser and the new throttle together with a high pressure generator, a vaporizer, an absorber, a first solution pump and the like construct a single effect flow so as to form a single effect flow heat supply end; the newly added absorber, the absorption vaporizer, the solution pump, the refrigerant liquid pump or the second throttle and the like together with the high pressure generator, the newly added condenser, the newly added throttle and the vaporizer construct an adjacent high temperature flow heat supply end of the single effect flow, so as to form a multiple compound of double effect flow, single effect flow and two-stage flow; in like manner, a multiple compound comprising triple effect flow, double effect flow, single effect flow and two-stage flow can be obtained; the invention improves the performance index of the heat pump in the corresponding temperature range of the multiple flow, can utilize afterheat during refrigeration, and can realize conversion and cooperation between the various flows.

Description

Multiple compound first class absorption heat pump

Technical field:

The invention belongs to low temperature exhaust heat utilization and absorption type heat pump.

Background technology:

Simple in structure, performance index is high, can satisfy the demands and a machine double-purpose (or many with) is the direction and the requirement of absorption heating/Refrigeration Technique development.When carrying out the heat utilization of waste heat; The relation that mutual restriction is arranged between the running parameter of unit and its performance index: imitate in the single-stage unit between the different unit of number and compare; The heat supply temperature height of single-action unit but performance index is low, the performance index height of economic benefits and social benefits unit but heat supply temperature is low; Compare between the unit of different progression, the unit heat supply temperature that progression is low is low but performance index high, the unit heat supply temperature height that progression is high but performance index is low.Simultaneously; To the single unit of confirming---like single-stage single-action, single-stage economic benefits and social benefits or single-stage, two-stage unit etc.; Because receive the restriction of unit self-condition (idiographic flow, SOLUTION PROPERTIES etc.) and external condition (like residual heat resources), the unit of single structure can only satisfy the demand of heated medium certain limit.Lower when the initial temperature of heated medium, finishing temperature is higher and when crossing over the unit of two above heating ranges, then need adopt the MULTIPLE COMPOSITE unit to reach the purpose that energy-saving benefit maximization, set structure are oversimplified.

In demand parameter (especially temperature) occasion that amplitude of variation is bigger of heated medium, unit should be according to the demand for heat adjustment operational mode of the maximized principle of performance index according to heated medium.In addition; Occasion such as heat supply that needs higher temperature winter and summer cooling; Unit in the winter time will be according to the MULTIPLE COMPOSITE mode operation to provide the heating parameter of higher temperature as heat pump; And unit need be according to economic benefits and social benefits or multiple-effect process flow operation to obtain higher performance index when freezing summer, and this needs a cover unit can realize the conversion between the different flow processs.

Maximize and realize the conversion between the different flow processs as far as possible for what when meeting consumers' demand, realize the unit performance index; Consider the simplification of heat pump/refrigerating system simultaneously; In same unit, realize effectively and reasonably compound of heat pump/refrigerating flow process, realize that MULTIPLE COMPOSITE absorption heat pump/cooling flow is highly significant.

Summary of the invention:

Main purpose of the present invention is that multiple compound first class absorption heat pump will be provided; It is characterized in that on the basis of double effect absorption type heat pump increasing newly-increased parts---newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger or add and increase second solution heat exchanger newly; Form single-stage high-temperature heat supply end adjacent and the two-stage high-temperature heat supply end adjacent successively, form single-stage economic benefits and social benefits, single-stage single-action and the compound triple composite absorption heat pumps of two-stage three flow processs with single-stage process flow with double-effect process; On the basis of three-effect absorption-type heat pump, increase newly-increased parts---newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger or add increase newly second solution heat exchanger, again increase condenser, increase choke valve again; Form the economic benefits and social benefits heat supply end adjacent, the single-action heat supply end adjacent and the two-stage heat supply end adjacent successively, composition single-stage triple effect, single-stage economic benefits and social benefits, single-stage single-action and the compound quadruple composite absorption heat pump of two-stage four flow processs with single-action with the economic benefits and social benefits temperature end with the triple effect heat pump flowsheet.

1. one of triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis among the present invention are achieved in that in the solution series circulation single-stage economic benefits and social benefits first kind absorption heat pump of being made up of high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, second solution pump, solution heat exchanger and second solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by high pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with high pressure generator through newly-increased solution pump, newly-increased solution heat exchanger with newly-increased second solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original double-effect process heat supply end; Newly-increased condenser is newly-increased single-stage process flow heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by high pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with low pressure generator with second solution heat exchanger through solution pump, solution heat exchanger absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with second solution heat exchanger through solution pump, solution heat exchanger to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with low pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original double-effect process heat supply end; Newly-increased condenser is newly-increased single-stage process flow heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

2. two of the triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis among the present invention is such realizations: in the solution series circulation single-stage economic benefits and social benefits first kind absorption heat pump of being made up of high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, solution heat exchanger and second solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by high pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with high pressure generator through newly-increased solution pump, newly-increased solution heat exchanger with newly-increased second solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original double-effect process heat supply end; Newly-increased condenser is newly-increased single-stage process flow heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by high pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator with second solution heat exchanger through solution pump, solution heat exchanger absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with second solution heat exchanger through solution pump, solution heat exchanger to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with high pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original double-effect process heat supply end; Newly-increased condenser is newly-increased single-stage process flow heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

3. the triple composite absorption heat pump (type I)s on the parallel connection of the solution among the present invention circulation economic benefits and social benefits basis are achieved in that in the solution parallel connection circulation single-stage economic benefits and social benefits first kind absorption heat pump of being made up of high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, solution heat exchanger and second solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by high pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with high pressure generator through newly-increased solution pump, newly-increased solution heat exchanger with newly-increased second solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original double-effect process heat supply end; Newly-increased condenser is newly-increased single-stage process flow heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution parallel connection circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by high pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator with solution heat exchanger through solution pump absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with solution heat exchanger through solution pump to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with high pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up the cryogen liquid pipeline by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or is set up the cryogen liquid pipeline by newly-increased condenser through newly-increased absorptions-evaporimeter behind the logical newly-increased absorptions-evaporimeter of newly-increased cryogen liquid pump and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original double-effect process heat supply end; Newly-increased condenser is newly-increased single-stage process flow heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution parallel connection circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

4. one of triple composite absorption heat pump (type I)s on the solution series circulation three-effect basis among the present invention are achieved in that in the solution series circulation single-stage triple-effect first category absorption heat pump of being made up of high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, second solution pump, the 3rd solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to press generator through newly-increased solution pump, newly-increased solution heat exchanger and during newly-increased second solution heat exchanger is communicated with; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Newly-increased absorber is newly-increased single-action flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with low pressure generator with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with low pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Newly-increased absorber is newly-increased single-action flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process.

5. two of the triple composite absorption heat pump (type I)s on the solution series circulation three-effect basis among the present invention be achieved in that in the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to press generator through newly-increased solution pump, newly-increased solution heat exchanger and during newly-increased second solution heat exchanger is communicated with; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Newly-increased absorber is newly-increased single-action flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with high pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Newly-increased absorber is newly-increased single-action flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process.

6. the triple composite absorption heat pump (type I)s on the parallel connection of the solution among the present invention circulation three-effect basis are achieved in that in the solution parallel connection circulation single-stage triple-effect first category absorption heat pump of being made up of high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to press generator through newly-increased solution pump, newly-increased solution heat exchanger and during newly-increased second solution heat exchanger is communicated with; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Newly-increased absorber is newly-increased single-action flow process heat supply end, thereby obtains comprising on the solution parallel connection circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Again with absorber have the weak solution pipeline through solution pump with press during second solution heat exchanger is communicated with generator to change absorber into to have the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with second solution heat exchanger to have the weak solution pipeline after newly-increased solution heat exchanger is communicated with newly-increased absorption-evaporimeter, to increase absorption-evaporimeter newly again to have weak solution pipeline warp to increase solution pump newly again and press generator during newly-increased solution heat exchanger is communicated with through solution pump; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Set up that cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or set up the cryogen liquid pipeline by newly-increased condenser by evaporimeter and increase absorption-evaporimeter newly after the connection of second choke valve increases absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again through increasing newly, newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Newly-increased absorber is newly-increased single-action flow process heat supply end, thereby obtains comprising on the solution parallel connection circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process.

7. one of quadruple composite absorption heat pump (type I) on the solution series circulation three-effect basis among the present invention is achieved in that in the solution series circulation single-stage triple-effect first category absorption heat pump of being made up of high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, second solution pump, the 3rd solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger, increase second solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator again and increase condenser again; Increase condenser again or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser or newly-increased condenser, increase condenser again and also have heated medium pipeline and external communications through increasing choke valve again through increasing choke valve again; Set up the concentrated solution pipeline from high pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with high pressure generator through newly-increased solution pump, newly-increased solution heat exchanger with newly-increased second solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or sets up the cryogen liquid pipeline and after newly-increased second choke valve connection increases absorption-evaporimeter newly, increase absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again by increasing condenser again, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Increase condenser again and be newly-increased single-action flow process heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator again and increase condenser again; Increase condenser again or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser or newly-increased condenser, increase condenser again and also have heated medium pipeline and external communications through increasing choke valve again through increasing choke valve again; Having the weak solution pipeline to be communicated with low pressure generator with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with low pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or sets up the cryogen liquid pipeline and after newly-increased second choke valve connection increases absorption-evaporimeter newly, increase absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again by increasing condenser again, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Increase condenser again and be newly-increased single-action flow process heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

8. one of quadruple composite absorption heat pump (type I) on the solution series circulation three-effect basis among the present invention is achieved in that in the solution series circulation single-stage triple-effect first category absorption heat pump of being made up of high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger, increase second solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator again and increase condenser again; Increase condenser again or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser or newly-increased condenser, increase condenser again and also have heated medium pipeline and external communications through increasing choke valve again through increasing choke valve again; Set up the concentrated solution pipeline from high pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with high pressure generator through newly-increased solution pump, newly-increased solution heat exchanger with newly-increased second solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or sets up the cryogen liquid pipeline and after newly-increased second choke valve connection increases absorption-evaporimeter newly, increase absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again by increasing condenser again, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Increase condenser again and be newly-increased single-action flow process heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator again and increase condenser again; Increase condenser again or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser or newly-increased condenser, increase condenser again and also have heated medium pipeline and external communications through increasing choke valve again through increasing choke valve again; Having the weak solution pipeline to be communicated with high pressure generator with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with the 3rd solution heat exchanger through solution pump, solution heat exchanger, second solution heat exchanger to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with high pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or sets up the cryogen liquid pipeline and after newly-increased second choke valve connection increases absorption-evaporimeter newly, increase absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again by increasing condenser again, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Increase condenser again and be newly-increased single-action flow process heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

9. the quadruple composite absorption heat pump (type I) on the parallel connection of the solution among the present invention circulation three-effect basis is achieved in that in the solution parallel connection circulation single-stage triple-effect first category absorption heat pump of being made up of high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger, increase second solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator again and increase condenser again; Increase condenser again or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser or newly-increased condenser, increase condenser again and also have heated medium pipeline and external communications through increasing choke valve again through increasing choke valve again; Set up the concentrated solution pipeline from high pressure generator again and be communicated with newly-increased absorber through newly-increased second solution heat exchanger; Newly-increased absorber has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter through newly-increased solution heat exchanger; Newly-increased absorption-evaporimeter also has the weak solution pipeline to be communicated with high pressure generator through newly-increased solution pump, newly-increased solution heat exchanger with newly-increased second solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or sets up the cryogen liquid pipeline and after newly-increased second choke valve connection increases absorption-evaporimeter newly, increase absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again by increasing condenser again, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Increase condenser again and be newly-increased single-action flow process heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution parallel connection circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser of refrigerant vapour pipeline connection by middle pressure generator; There is the cryogen liquid pipeline in the 3rd choke valve connection condenser changes into, to press generator to have the cryogen liquid pipeline to be communicated with in middle pressure generator and increases condenser newly through the 3rd choke valve; Increase condenser newly or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser through increasing choke valve newly through newly-increased choke valve, newly-increased condenser also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator again and increase condenser again; Increase condenser again or have the cryogen liquid pipeline to be communicated with evaporimeter or to have the cryogen liquid pipeline to be communicated with condenser or newly-increased condenser, increase condenser again and also have heated medium pipeline and external communications through increasing choke valve again through increasing choke valve again; Having the weak solution pipeline to be communicated with high pressure generator with solution heat exchanger through solution pump absorber again changes absorber into and has the weak solution pipeline to be communicated with newly-increased absorber, newly-increased absorber with solution heat exchanger through solution pump to have weak solution pipeline newly-increased absorption-evaporimeter after newly-increased solution heat exchanger is communicated with newly-increased absorptions-evaporimeter to have weak solution pipeline warp to increase solution pump newly more again to be communicated with high pressure generator with newly-increased solution heat exchanger; Set up the newly-increased absorption-evaporimeter of refrigerant vapour pipeline connection by evaporimeter; Setting up cryogen liquid pipeline newly-increased absorptions-evaporimeter after newly-increased cryogen liquid pump is communicated with newly-increased absorptions-evaporimeter by evaporimeter has the newly-increased absorber of refrigerant vapour pipeline connection again or sets up the cryogen liquid pipeline and after newly-increased second choke valve connection increases absorption-evaporimeter newly, increase absorption-evaporimeter newly and have the refrigerant vapour pipeline connection to increase absorber newly again by increasing condenser again, and newly-increased absorber also has heated medium pipeline and external communications; Absorber and condenser are original triple effect flow process heat supply end; Newly-increased condenser is newly-increased double-effect process heat supply end; Increase condenser again and be newly-increased single-action flow process heat supply end; Newly-increased absorber is newly-increased two-stage flow process heat supply end, thereby obtains comprising on the solution parallel connection circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

10. in the triple composite absorption heat pump (type I)s on the economic benefits and social benefits basis of addressing in front; Increase heated medium branch line and bypass line; And on heated medium pipeline and bypass line, increase by first control valve (f1), second control valve, the 3rd control valve (f3), the 4th control valve (f4), the 5th control valve (f5) and the 6th control valve (f6); Setting up its bypass line on the heated medium pipeline between condenser (C1) and the newly-increased condenser, setting up its branch line, increasing by first control valve (f1) on the heated medium pipeline, increasing by second control valve on the bypass line, setting up the 3rd control valve (f3) on the branch line and on the heated medium pipeline between newly-increased condenser and the newly-increased absorber, setting up its bypass line, setting up its branch line at newly-increased condensator outlet in condenser (C1) outlet, at increase the 5th control valve (f5) on the heated medium pipeline, at increase the 6th control valve (f6) on the bypass line, on newly-increased condensator outlet branch line, set up the 4th control valve (f4), accomplished single-action, economic benefits and social benefits and triple effect are mutual cooperates or triple composite absorption heat pump (type I)s of conversion.

Description of drawings:

At first be noted that; In the description of drawings below; The multiple compound first class absorption heat pump of same names has adopted numercal different layout, same names and the difference of different digital layout shows three aspects: 1. the existing heat pump structure as basic flow process is different with idiographic flow; 2. newly-increased solution flow process is different; 3. the flow process of newly-increased cryogen liquid is different.The description in the specific embodiment is seen in concrete difference between them.

Fig. 1 is according to the 1st triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting the solution series circulation, form.

Fig. 2 is according to the 2nd triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting the solution series circulation, form.

Fig. 3 is according to the 3rd triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting the solution series circulation, form.

Fig. 4 is according to the 4th triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting the solution series circulation, form.

Fig. 5 is according to the 5th triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting the solution series circulation, form.

Fig. 6 is according to the 1st triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting solution parallel connection circulation, form.

Fig. 7 is according to the 2nd triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the double effect absorption type heat pump basis of adopting solution parallel connection circulation, form.

Fig. 8 is according to the 1st triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Fig. 9 is according to the 2nd triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 10 is according to the 3rd triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 11 is according to the 4th triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 12 is according to the 1st triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting solution parallel connection circulation, form.

Figure 13 is according to the 2nd triple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting solution parallel connection circulation, form.

Figure 14 is according to the 1st quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 15 is according to the 2nd quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 16 is according to the 3rd quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 17 is according to the 4th quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 18 is according to the 5th quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form.

Figure 19 is according to the 1st quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting solution parallel connection circulation, form.

Figure 20 is according to the 2nd quadruple composite absorption heat pump (type I) structure and schematic flow sheet provided by the present invention, that on the three-effect absorption-type heat pump basis of adopting solution parallel connection circulation, form.

Figure 21 be according to provided by the present invention, on the three-effect absorption-type heat pump basis of adopting the solution series circulation, form, can realize mutual the cooperating or change triple composite absorption heat pump (type I) structures and schematic flow sheet of single-action, economic benefits and social benefits and triple effect.

Among the figure, 1-increases condenser newly, and 2-increases choke valve newly, and 3-increases absorber newly; 4-increases absorption-evaporimeter newly, and 5-increases the cryogen liquid pump newly, and 6-increases second choke valve newly, and 7-increases solution pump newly; 8-increases solution heat exchanger newly, and 9-increases second solution heat exchanger newly, and 10-increases condenser again, and 11-increases choke valve again.

Among Fig. 1-Fig. 7, Figure 21, A1-high pressure generator, B1-low pressure generator, C1-condenser, D1-evaporimeter, E1-absorber, F1-choke valve, G1-second choke valve, H1-solution pump, I1-second solution pump, J1-solution heat exchanger, K1-second solution heat exchanger; F1-first control valve, f2-second control valve, f3-the 3rd control valve, f4-the 4th control valve, f5-the 5th control valve, f6-the 6th control valve.

Among Fig. 8-Figure 20, the A2-high pressure generator is pressed generator among the B2-, the C2-low pressure generator; The D2-condenser, E2-evaporimeter, F2-absorber, G2-solution pump; H2-second solution pump, I2-the 3rd solution pump, J2-choke valve, K2-second choke valve; L2-the 3rd choke valve, M2-solution heat exchanger, N2-second solution heat exchanger, O2-the 3rd solution heat exchanger.

The specific embodiment:

Describe the present invention in detail below in conjunction with accompanying drawing and instance.

The purpose that on the single-stage double effect absorption type heat pump basis of adopting the solution series circulation, forms triple composite absorption heat pump (type I)s shown in Figure 1 is achieved in that

1. on the structure; In the single-stage economic benefits and social benefits first kind absorption heat pump that high pressure generator A1, low pressure generator B1, condenser C1, evaporimeter D1, absorber E1, solution pump H1, the second solution pump I1, choke valve F1, the second choke valve G1, solution heat exchanger J1 and the second solution heat exchanger K1 form, solution series circulates; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by high pressure generator A1; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter D1 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline by high pressure generator A1 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A1 through newly-increased solution pump 7, newly-increased solution heat exchanger 8, newly-increased second solution heat exchanger 9; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter D1; Evaporimeter D1 also sets up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process; The new single-stage single-action heat pump flowsheet that newly-increased 1 pair of heated medium of condenser carries out heat supply is performed such: high pressure generator A1, newly-increased condenser 1, newly-increased choke valve 2, evaporimeter D1, absorber E1, solution pump H1 and solution heat exchanger J1 and piggybacking constitute new single-stage single-action heat pump flowsheet in low pressure generator B1, the second solution heat exchanger K1 and the second solution pump I1---and the solution that is got into high pressure generator A1 by the low pressure generator B1 warp second solution heat exchanger K1 and the second solution pump I1 externally drives the refrigerant vapour that discharges under the effect of heat; Part refrigerant vapour gets into the laggard evaporimeter D1 of going into of the corresponding flow process of low pressure generator B1 participation economic benefits and social benefits and absorbs heat into refrigerant vapour; Behind the heated medium of flowing through in it, become cryogen liquid and make newly-increased condenser 1 become the adjacent high-temperature heat supply end of single-stage double-effect process thereby another part refrigerant vapour gets into newly-increased condenser 1 heat release; Newly-increased condenser 1 interior cryogen liquid gets into evaporimeter D1 absorption waste heat through newly-increased choke valve 2 throttling step-downs cooling and becomes refrigerant vapour; Absorbing above-mentioned two parts steam from the concentrated solution of high pressure generator A1 in the absorber E1 becomes weak solution and heat release in the heated medium of flowing through in it; Weak solution is heated through solution pump H1 pressurization entering low pressure generator B1 and is discharged the refrigerant medium of participating in double-effect process, discharges the refrigerant medium of participating in the single-action flow process under the solution entering high pressure generator A1 after concentration improves and the effect of externally driving heat; Newly-increased 3 pairs of heated mediums of absorber carry out that the new two-stage heat pump flowsheet of heat supply is performed such: high pressure generator A1, newly-increased condenser 1, evaporimeter D1, newly-increased cryogen liquid pump 5, newly-increased absorptions-evaporimeter 4, newly-increased absorber 3, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9 constitute new two-stage heat pump flowsheet---high pressure generator A1 concentrated solution through newly-increased second solution heat exchanger 9 get into newly-increased absorber 3, absorption from the refrigerant vapour that increases absorption-evaporimeter 4 newly after heat release in heated medium; Solution after concentration reduce in the newly-increased absorber 3 after newly-increased solution heat exchanger 8 gets into the refrigerant vapour that newly-increased absorption-evaporimeter 4, absorption come flash-pot D1 heat release in the refrigerant medium of flowing through in it; Solution after concentration further reduces in the newly-increased absorption-evaporimeter 4 gets into high pressure generator A1 through newly-increased solution pump 7, newly-increased solution heat exchanger 8, newly-increased second solution heat exchanger 9; The effect that the weak solution that gets into high pressure generator A1 externally drives heat discharges down that refrigerant vapour gets into newly-increased condenser 1, heat release becomes cryogen liquid behind heated medium, and the part after newly-increased choke valve 2 throttlings get into evaporimeter D1 of this part cryogen liquid in the newly-increased condenser 1 is absorbed heat into refrigerant vapour and got into newly-increased absorptions-evaporimeter 4, another part warp and increase cryogen liquid pump 5 newly and squeeze into and increase absorption-evaporimeter 4 newly and absorb heat into refrigerant vapour and provide to newly-increased absorber 3; Single-action, double-effect process common suction device E1; Single-stage (also being single-action), the shared newly-increased condenser 1 of two-stage flow process; Newly-increased single-stage single-action flow process, two-stage flow process and original single-stage double-effect process are formed triple composite absorption heat pump (type I) flow processs, and the absorber E1 of complex flow and condenser C1, newly-increased condenser 1 and newly-increased absorber 3 are respectively to the heated medium heat supply.

The triple composite absorption heat pump (type I)s that in the double effect absorption type heat pump that adopts the solution series circulation, form on the basis shown in Figure 2 are achieved in that

1. on the structure; In the single-stage economic benefits and social benefits first kind absorption heat pump that high pressure generator A1, low pressure generator B1, condenser C1, evaporimeter D1, absorber E1, solution pump H1, the second solution pump I1, choke valve F1, the second choke valve G1, solution heat exchanger J1 and the second solution heat exchanger K1 form, solution series circulates; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and increase second solution heat exchanger 9 newly; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by high pressure generator A1; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser C1 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline by high pressure generator A1 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A1 through newly-increased solution pump 7, newly-increased solution heat exchanger 8, newly-increased second solution heat exchanger 9; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter D1; Newly-increased condenser 1 also has cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased second choke valve 6 is communicated with newly-increased absorption-evaporimeter 4 to have the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process; The new single-stage heat pump flowsheet that newly-increased 1 pair of heated medium of condenser carries out heat supply is performed such: high pressure generator A1, newly-increased condenser 1, newly-increased choke valve 2, evaporimeter D1, absorber E1, solution pump H1 and solution heat exchanger J1 and piggybacking constitute new single-stage single-action heat pump flowsheet in condenser C1 and choke valve F1, low pressure generator B1, the second solution heat exchanger K1 and the second solution pump I1---and the solution that is got into high pressure generator A1 by the low pressure generator B1 warp second solution heat exchanger K1 and the second solution pump I1 externally drives the refrigerant vapour that discharges under the effect of heat; Part refrigerant vapour gets into the laggard evaporimeter D1 of going into of the corresponding flow process of low pressure generator B1 participation economic benefits and social benefits and absorbs heat into refrigerant vapour; Behind the heated medium of flowing through in it, become cryogen liquid and make newly-increased condenser 1 become the adjacent high-temperature heat supply end of single-stage double-effect process thereby another part refrigerant vapour gets into newly-increased condenser 1 heat release; Choke valve 2 throttling step-downs cooling gets into condenser C1, entering evaporimeter D1 absorption waste heat becomes refrigerant vapour after choke valve F1 throttling again through increasing newly to increase condenser 1 interior cryogen liquid newly; Absorbing above-mentioned two parts steam from the concentrated solution of high pressure generator A1 in the absorber E1 becomes weak solution and heat release in the heated medium of flowing through in it; Weak solution is heated through solution pump H1 pressurization entering low pressure generator B1 and is discharged the refrigerant medium of participating in double-effect process, discharges the refrigerant medium of participating in the single-action flow process under the solution entering high pressure generator A1 after concentration improves and the effect of externally driving heat; Newly-increased 3 pairs of heated mediums of absorber carry out that the new two-stage heat pump flowsheet of heat supply is performed such: high pressure generator A1, newly-increased condenser 1, evaporimeter D1, newly-increased second choke valve 6, newly-increased absorptions-evaporimeter 4, newly-increased absorber 3, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9 and piggybacking constitute new two-stage heat pump flowsheet in newly-increased choke valve 2, condenser C1 and choke valve F1---the concentrated solution of high pressure generator A1 through newly-increased second solution heat exchanger 9 get into newly-increased absorber 3, absorption from the refrigerant vapour that increases absorption-evaporimeter 4 newly after heat release in heated medium; Solution after concentration reduce in the newly-increased absorber 3 after newly-increased solution heat exchanger 8 gets into the refrigerant vapour that newly-increased absorption-evaporimeter 4, absorption come flash-pot D1 heat release in the refrigerant medium of flowing through in it; Solution after concentration further reduces in the newly-increased absorption-evaporimeter 4 gets into high pressure generator A1 through newly-increased solution pump 7, newly-increased solution heat exchanger 8, newly-increased second solution heat exchanger 9; The effect that the weak solution that gets into high pressure generator A1 externally drives heat discharges down that refrigerant vapour gets into newly-increased condenser 1, heat release becomes cryogen liquid behind heated medium, and the cryogen liquid in the newly-increased condenser 1 is divided into two parts---a part through get into after newly-increased second choke valve, 6 throttlings newly-increased absorptions-evaporimeter 4 absorb heat into refrigerant vapour to newly-increased absorber 3 provide, another part absorbs heat into refrigerant vapour through choke valve F1 throttling entering evaporimeter D1 again after increasing choke valve 2 throttlings entering condenser C1 newly provide to newly-increased absorption-evaporimeter 4; Single-action, double-effect process common suction device E1; Single-stage, the shared newly-increased condenser 1 of two-stage flow process; Newly-increased single-stage single-action flow process, two-stage flow process and original single-stage double-effect heat pump flow process are formed triple composite absorption heat pump (type I) flow processs, and absorber E1 and condenser C1, newly-increased condenser 1 and newly-increased absorber 3 are respectively to the heated medium heat supply.

Above-mentioned heat pump flowsheet also can be described like this: the heat supply of newly-increased condenser 1 derives from the refrigerant vapour of high pressure generator A1, is the single-action thermal loads; The solution of newly-increased absorber 3 from high pressure generator A1, refrigerant vapour from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once---it plays conclusive effect to the thermal performance of newly-increased absorber 3, is one generator type two-stage heat pump flowsheet; So then form the triple composite absorption heat pump (type I) flow processs that comprise original double-effect process, newly-increased single-action flow process and newly-increased two-stage flow process, thereby obtained the triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis.

The triple composite absorption heat pump (type I)s that in the double effect absorption type heat pump that adopts the solution series circulation, form on the basis shown in Figure 3 are achieved in that

1. on the structure; In the single-stage economic benefits and social benefits first kind absorption heat pump that high pressure generator A1, low pressure generator B1, condenser C1, evaporimeter D1, absorber E1, solution pump H1, choke valve F1, the second choke valve G1, solution heat exchanger J1 and the second solution heat exchanger K1 form, solution series circulates; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, increase solution pump 7 and newly-increased solution heat exchanger 8 newly; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by high pressure generator A1; Newly-increased condenser 1 has the cryogen liquid pipeline to be communicated with evaporimeter D1 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with low pressure generator B1 with the second solution heat exchanger K1 through solution pump H1, solution heat exchanger J1 absorber E1 again changes absorber E1 into and has the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with the second solution heat exchanger K1 through solution pump H1, solution heat exchanger J1 to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter 4 back through newly-increased solution heat exchanger 8 again to increase absorption-evaporimeter 4 newly and have weak solution pipeline warp to increase solution pump 7 newly again to be communicated with low pressure generator B1 with newly-increased solution heat exchanger 8; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter D1; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased second choke valve 6 is communicated with newly-increased absorption-evaporimeter 4 by newly-increased condenser 1 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process, the heat supply of newly-increased condenser 1 derives from the refrigerant vapour of high pressure generator A1, is the single-action thermal loads; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, is one generator type two-stage heat pump flowsheet from absorber E1, refrigerant vapour; So then form the triple composite absorption heat pump (type I) flow processs that comprise original double-effect process, newly-increased single-action flow process and newly-increased two-stage flow process, thereby obtained the triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis.

The triple composite absorption heat pump (type I)s that in the double effect absorption type heat pump that adopts the solution series circulation, form on the basis shown in Figure 4 are achieved in that

1. on the structure; In the single-stage economic benefits and social benefits first kind absorption heat pump that high pressure generator A1, low pressure generator B1, condenser C1, evaporimeter D1, absorber E1, solution pump H1, choke valve F1, the second choke valve G1, solution heat exchanger J1 and the second solution heat exchanger K1 form, solution series circulates; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by high pressure generator A1; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser C1 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline by high pressure generator A1 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A1 through newly-increased solution pump 7, newly-increased solution heat exchanger 8, newly-increased second solution heat exchanger 9; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter D1; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 by evaporimeter D1 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process, the heat supply of newly-increased condenser 1 derives from the refrigerant vapour of high pressure generator A1, is the single-action thermal loads; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, is one generator type two-stage heat pump flowsheet from high pressure generator A1, refrigerant vapour; So then form the triple composite absorption heat pump (type I) flow processs that comprise original double-effect process, newly-increased single-action flow process and newly-increased two-stage flow process, thereby obtained the triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis.

The triple composite absorption heat pump (type I)s that in the double effect absorption type heat pump that adopts the solution series circulation, form on the basis shown in Figure 5; Compare with shown in Figure 4; The difference of the two is---1. newly-increased condenser 1 has the cryogen liquid pipeline to be communicated with condenser C1 through newly-increased choke valve 2 among Fig. 4, and newly-increased condenser 1 has the cryogen liquid pipeline to be communicated with evaporimeter D1 through newly-increased choke valve 2 among Fig. 5; 2. evaporimeter D1 sets up the cryogen liquid pipeline and is communicated with the newly-increased absorptions-evaporimeter 4 in newly-increased absorptions-evaporimeter 4 back through newly-increased cryogen liquid pump 5 and has the refrigerant vapour pipeline connection increase absorber 3 again among Fig. 4, then is that newly-increased condenser 1 has the cryogen liquid pipeline to increase absorption-evaporimeter 4 newly after 6 connections of second choke valve increase absorption-evaporimeter 4 newly and have the refrigerant vapour pipeline connection to increase absorber 3 newly again through increasing newly among Fig. 5; 3. to newly-increased absorber 3 solution is provided by high pressure generator A1 among Fig. 4, among Fig. 5 then by absorber E1 to solution being provided to newly-increased absorber 3.

The triple composite absorption heat pump (type I)s that in the double effect absorption type heat pump that adopts solution parallel connection circulation, form on the basis shown in Figure 6 are achieved in that

1. on the structure; In the solution parallel connection circulation single-stage economic benefits and social benefits first kind absorption heat pump of forming by high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, solution heat exchanger and second solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and increase second solution heat exchanger 9 newly; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by high pressure generator A1; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser C1 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator A1 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A1 through newly-increased solution pump 7, newly-increased solution heat exchanger 8 with newly-increased second solution heat exchanger 9; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter D1; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased second choke valve 6 is communicated with newly-increased absorption-evaporimeter 4 by newly-increased condenser 1 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process; Newly-increased single-action flow process is performed such: externally drive the refrigerant vapour that discharges under the effect of heat by absorber E1 through the solution that solution pump H1, solution heat exchanger J1 get into high pressure generator A1; A part gets into the laggard evaporimeter D1 of going into of the corresponding flow process of low pressure generator B1 participation economic benefits and social benefits and absorbs heat into refrigerant vapour; Another part gets into newly-increased condenser 1 heat release becomes the adjacent high-temperature heat supply end that cryogen liquid forms the single-stage double-effect process behind the heated medium of flowing through in it; Choke valve 2 throttling step-downs cooling gets into condenser C1, entering evaporimeter D1 absorption waste heat becomes refrigerant vapour after choke valve F1 throttling again through increasing newly to increase condenser 1 interior cryogen liquid newly; Absorb above-mentioned two parts steam from the concentrated solution of high pressure generator A1 in the absorber E1 and become weak solution and heat release in the heated medium of flowing through in it, weak solution gets into high pressure generator A1 through solution pump H1 pressurization and is heated and discharges refrigerant medium of participating in double-effect process and the refrigerant medium of participating in the single-action flow process; The solution of newly-increased absorber 3 from high pressure generator A1, refrigerant vapour from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once; Be one generator type two-stage heat pump flowsheet; So then form the triple composite absorption heat pump (type I) flow processs that comprise original double-effect process, newly-increased single-action flow process and newly-increased two-stage flow process, obtained comprising on the solution parallel connection circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

The triple composite absorption heat pump (type I)s that in the double effect absorption type heat pump that adopts solution parallel connection circulation, form on the basis shown in Figure 7; Compare with shown in Figure 6; The difference of the two is---1. evaporimeter D1 sets up the cryogen liquid pipeline and is communicated with the newly-increased absorptions-evaporimeter 4 in newly-increased absorptions-evaporimeter 4 back through newly-increased cryogen liquid pump 5 and has the refrigerant vapour pipeline connection increase absorber 3 again among Fig. 7, then is that newly-increased condenser 1 has the cryogen liquid pipeline to increase absorption-evaporimeter 4 newly after 6 connections of second choke valve increase absorption-evaporimeter 4 newly and have the refrigerant vapour pipeline connection to increase absorber 3 newly again through increasing newly among Fig. 6; 2. to newly-increased absorber 3 solution is provided by high pressure generator A1 among Fig. 6, among Fig. 7 then by absorber E1 to solution being provided to newly-increased absorber 3.

The triple composite absorption heat pump (type I)s that in the three-effect absorption-type heat pump that adopts the solution series circulation, form on the basis shown in Figure 8 are achieved in that

1. on the structure; In the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, second solution pump, the 3rd solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter E2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator B2 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to press generator B2 through newly-increased solution pump 7, newly-increased solution heat exchanger 8 and during newly-increased second solution heat exchanger 9 is communicated with; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 by evaporimeter E2 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process, press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; From waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, its resultant effect is equivalent to be the single-stage heat pump flowsheet to the solution of newly-increased absorber 3 from middle pressure generator B2, refrigerant vapour; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process and newly-increased single-stage process flow have so then been formed, from obtaining triple composite absorption heat pump (type I)s that solution series circulation three-effect basis comprises triple effect flow process, double-effect process and single-action flow process.

The triple composite absorption heat pump (type I)s that in the three-effect absorption-type heat pump that adopts the solution series circulation, form on the basis shown in Figure 9 are achieved in that

In the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, second solution pump, the 3rd solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7 and newly-increased solution heat exchanger 8; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser D2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with low pressure generator C2 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 absorber F2 again changes absorber F2 into and has the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter 4 back through newly-increased solution heat exchanger 8 again to increase absorption-evaporimeter 4 newly and have weak solution pipeline warp to increase solution pump 7 newly again to be communicated with low pressure generator C2 with newly-increased solution heat exchanger 8; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 again by evaporimeter E2 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The solution of newly-increased absorber 3 is from absorber F2---and it has part single-action thermic load, refrigerant vapour from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once; Its resultant effect is equivalent to be the single-stage heat pump flowsheet; So then formed the triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process and newly-increased single-stage process flow, the basis comprises triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process from the three-effect absorption-type heat pump that obtains the solution series circulation.

The triple composite absorption heat pump (type I)s that in the three-effect absorption-type heat pump that adopts the solution series circulation, form on the basis shown in Figure 10 are achieved in that

In the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter E2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator B2 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to press generator B2 through newly-increased solution pump 7, newly-increased solution heat exchanger 8 and during newly-increased second solution heat exchanger 9 is communicated with; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 by evaporimeter E2 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; From waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, its resultant effect is equivalent to be the single-stage heat pump flowsheet to the solution of newly-increased absorber 3 from middle pressure generator B2, refrigerant vapour; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process and newly-increased single-stage process flow have so then been formed, from obtaining triple composite absorption heat pump (type I)s that solution series circulation three-effect basis comprises triple effect flow process, double-effect process and single-action flow process.

The triple composite absorption heat pump (type I)s that in the three-effect absorption-type heat pump that adopts the solution series circulation, form on the basis shown in Figure 11 are achieved in that

In the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased choke valve 6, newly-increased solution pump 7 and newly-increased solution heat exchanger 8; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser D2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator A2 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 absorber F2 again changes absorber F2 into and has the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter 4 back through newly-increased solution heat exchanger 8 again to increase absorption-evaporimeter 4 newly and have weak solution pipeline warp to increase solution pump 7 newly again to be communicated with high pressure generator A2 with newly-increased solution heat exchanger 8; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2, setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased second choke valve 6 is communicated with newly-increased absorption-evaporimeter 4 by newly-increased condenser 1 has the refrigerant vapour pipeline connection to increase absorber 3 newly again; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; From waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, its resultant effect is equivalent to be the single-stage heat pump flowsheet to the solution of newly-increased absorber 3 from absorber F2, refrigerant vapour; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process and newly-increased single-stage process flow have so then been formed, from obtaining triple composite absorption heat pump (type I)s that solution series circulation three-effect basis comprises triple effect flow process, double-effect process and single-action flow process.

The triple composite absorption heat pump (type I)s that in the three-effect absorption-type heat pump that adopts solution parallel connection circulation, form on the basis shown in Figure 12 are achieved in that

In the solution parallel connection circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorption-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7 and newly-increased solution heat exchanger 8; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser D2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Again with absorber F2 have the weak solution pipeline through solution pump G2 with press during the second solution heat exchanger N2 is communicated with generator B2 to change absorber F2 into to have the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with the second solution heat exchanger N2 to have the weak solution pipeline after newly-increased solution heat exchanger 8 is communicated with newly-increased absorptions-evaporimeter 4, to increase absorption-evaporimeter 4 newly again to have weak solution pipeline warp to increase solution pump 7 newly again and pressure generator B2 during newly-increased solution heat exchanger 8 is communicated with through solution pump G2; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 by evaporimeter E2 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; From waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, its resultant effect is equivalent to be the single-stage heat pump flowsheet to the solution of newly-increased absorber 3 from absorber F2, refrigerant vapour; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process and newly-increased single-stage process flow have so then been formed, from obtaining triple composite absorption heat pump (type I)s that solution parallel connection circulation three-effect basis comprises triple effect flow process, double-effect process and single-action flow process.

The triple composite absorption heat pump (type I)s that in the three-effect absorption-type heat pump that adopts solution parallel connection circulation, form on the basis shown in Figure 13 are achieved in that

In the solution parallel connection circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and increase second solution heat exchanger 9 newly; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter E2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator B2 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to press generator B2 through newly-increased solution pump 7, newly-increased solution heat exchanger 8 and during newly-increased second solution heat exchanger 9 is communicated with; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased second choke valve 6 is communicated with newly-increased absorption-evaporimeter 4 by newly-increased condenser 1 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, is the single-stage heat pump flowsheet from middle pressure generator B2, refrigerant vapour; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process and newly-increased single-stage process flow have so then been formed, from obtaining triple composite absorption heat pump (type I)s that solution parallel connection circulation three-effect basis comprises triple effect flow process, double-effect process and single-action flow process.

The purpose that on the single-stage three-effect absorption-type heat pump basis of adopting the solution series circulation, forms the quadruple composite absorption heat pump (type I) shown in Figure 14 is achieved in that

1. on the structure; By high pressure generator A2, middle pressure generator B2, low pressure generator C2, condenser D2, evaporimeter E2, absorber F2, solution pump G2, the second solution pump H2, the 3rd solution pump I2, choke valve J2, the second choke valve K2, the 3rd choke valve L2, solution heat exchanger M2, the second solution heat exchanger N2 and the 3rd solution heat exchanger O2 forms, in the three-effect absorption-type heat pump of solution series circulation; Increase condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7, newly-increased solution heat exchanger 8 newly, increase second solution heat exchanger 9 newly, increase condenser 10 again and increase choke valve 11 again; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter E2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator A2 again and increase condenser 10 again, increase condenser 10 again and also have the cryogen liquid pipeline to be communicated with evaporimeter E2, increase condenser 10 again and also have heated medium pipeline and external communications through increasing choke valve 11 again; Set up the concentrated solution pipeline by high pressure generator A2 and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 also has the solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A2 through newly-increased solution pump 7, newly-increased solution heat exchanger 8, newly-increased second solution heat exchanger 9; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2 again; Evaporimeter E2 also sets up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications.

2. on the flow process; High pressure generator A2, middle pressure generator B2, newly-increased condenser 1, evaporimeter E2, absorber F2, the 3rd choke valve L2, newly-increased choke valve 2, solution pump G2, the second solution pump H2, solution heat exchanger M2 and the second solution heat exchanger N2 and piggybacking are formed single-stage double-effect heat pump flow process in low pressure generator C2, the 3rd solution heat exchanger O2 and the 3rd solution pump I2, and newly-increased condenser 1 is the adjacent heat supply end of single-stage triple effect heat pump flowsheet; High pressure generator A2, again increase condenser 10, evaporimeter E2, absorber F2, increase choke valve 11, solution pump G2 and solution heat exchanger M2 and piggybacking again and form single-stage single-action heat pump flowsheet in low pressure generator C2, the 3rd solution heat exchanger O2, the 3rd solution pump I2, middle pressure generator B2, the second solution heat exchanger N2, the second solution pump H2, increase the adjacent heat supply end of condenser 10 again for newly-increased single-stage double-effect heat pump flow process; High pressure generator A2, increase condenser 10, evaporimeter E2, newly-increased cryogen liquid pump 5, newly-increased absorptions-evaporimeter 4, newly-increased absorber 3, newly-increased solution pump 7, newly-increased solution heat exchanger 8 and newly-increased second solution heat exchanger 9 again and constitute new two-stage heat pump flowsheet, newly-increased absorber 3 is for increasing the adjacent heat supply end of single-stage heat pump flowsheet newly; Single-stage triple effect flow process, newly-increased single-stage double-effect process, newly-increased single-stage single-action flow process and newly-increased two-stage flow process are formed quadruple composite absorption heat pump (type I) flow process, the combined heat-pump flow process respectively absorber F2 with condenser D2, increase condenser 1 newly, increase condenser 10 and newly-increased absorber 3 to the heated medium heat supply again.

Shown in Figure 15; On the single-stage three-effect absorption-type heat pump basis of adopting the solution series circulation, form the quadruple composite absorption heat pump (type I); Be with the difference of comparing the two shown in Figure 14: 1. increasing condenser 10 among Figure 14 again and be communicated with evaporimeter E2 through increasing choke valve 11 again, then is to increase condenser 10 to be communicated with newly-increased condenser 1 through increasing choke valve 11 again among Figure 15; 2. evaporimeter E2 has cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 to have the refrigerant vapour pipeline connection to increase absorber 3 newly again among Figure 14, among Figure 16 then is to increase condenser 10 again to have cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased second choke valve 6 is communicated with newly-increased absorption-evaporimeter 4 to have the refrigerant vapour pipeline connection to increase absorber 3 newly again.

The purpose that on the single-stage three-effect absorption-type heat pump basis of adopting the solution series circulation, forms the quadruple composite absorption heat pump (type I) shown in Figure 16 is achieved in that

By high pressure generator A2, middle pressure generator B2, low pressure generator C2, condenser D2, evaporimeter E2, absorber F2, solution pump G2, the second solution pump H2, the 3rd solution pump I2, choke valve J2, the second choke valve K2, the 3rd choke valve L2, solution heat exchanger M2, the second solution heat exchanger N2 and the 3rd solution heat exchanger O2 forms, in the three-effect absorption-type heat pump of solution series circulation; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, newly-increased solution pump 7, increase solution heat exchanger 8 newly, increase condenser 10 again and increase choke valve 11 again; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter E2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator A2 again and increase condenser 10 again, increase condenser 10 again and also have the cryogen liquid pipeline to be communicated with evaporimeter E2, increase condenser 10 again and also have heated medium pipeline and external communications through increasing choke valve 11 again; Having the weak solution pipeline to be communicated with low pressure generator C2 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 absorber F2 again changes absorber F2 into and has the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter 4 back through newly-increased solution heat exchanger 8 again to increase absorption-evaporimeter 4 newly and have weak solution pipeline warp to increase solution pump 7 newly again to be communicated with low pressure generator C2 with newly-increased solution heat exchanger 8; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Set up the cryogen liquid pipeline and be communicated with the newly-increased absorption-evaporimeter 4 in newly-increased absorptions-evaporimeter 4 back through newly-increased second choke valve 6 and have the refrigerant vapour pipeline connection to increase absorber 3 newly again by increasing condenser 10 again, increase absorber 3 heated medium pipeline and external communications in addition newly; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The heat supply that increases condenser 10 again derives from the refrigerant vapour of high pressure generator A2, is single-action flow process thermic load; From waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, its heat supply temperature will surpass the heat supply temperature that increases condenser 10 again to the solution of newly-increased absorber 3, is equivalent to two-stage flow process thermic load from absorber F2, refrigerant vapour; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process, newly-increased single-stage process flow have so then been formed, from obtaining the quadruple composite absorption heat pump (type I) that solution series circulation three-effect basis comprises triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

The purpose that on the single-stage three-effect absorption-type heat pump basis of adopting the solution series circulation, forms the quadruple composite absorption heat pump (type I) shown in Figure 17 is achieved in that

By high pressure generator A2, middle pressure generator B2, low pressure generator C2, condenser D2, evaporimeter E2, absorber F2, solution pump G2, choke valve J2, the second choke valve K2, the 3rd choke valve L2, solution heat exchanger M2, the second solution heat exchanger N2 and the 3rd solution heat exchanger O2 forms, in the three-effect absorption-type heat pump of solution series circulation; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased cryogen liquid pump 5, newly-increased solution pump 7, newly-increased solution heat exchanger 8, increase second solution heat exchanger 9 newly, increase condenser 10 again and increase choke valve 11 again; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with evaporimeter E2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator A2 again and increase condenser 10 again, increase condenser 10 again and also have the cryogen liquid pipeline to be communicated with evaporimeter E2, increase condenser 10 again and also have heated medium pipeline and external communications through increasing choke valve 11 again; Set up the concentrated solution pipeline from high pressure generator A2 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 also has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A2 through newly-increased solution pump 7, newly-increased solution heat exchanger 8 with newly-increased second solution heat exchanger 9; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 by evaporimeter E2 has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The heat supply that increases condenser 10 again derives from the refrigerant vapour of high pressure generator A2, is single-action flow process thermic load; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, can be regarded one generator two-stage flow process thermic load from high pressure generator A2, refrigerant vapour as; The triple composite absorption heat pump (type I) flow processs that comprise original triple effect flow process, newly-increased double-effect process, newly-increased single-stage process flow have so then been formed, from obtaining the quadruple composite absorption heat pump (type I) that solution series circulation three-effect basis comprises triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

The purpose that on the single-stage three-effect absorption-type heat pump basis of adopting the solution series circulation, forms the quadruple composite absorption heat pump (type I) shown in Figure 180 is achieved in that

By high pressure generator A2, middle pressure generator B2, low pressure generator C2, condenser D2, evaporimeter E2, absorber F2, solution pump G2, choke valve J2, the second choke valve K2, the 3rd choke valve L2, solution heat exchanger M2, the second solution heat exchanger N2 and the 3rd solution heat exchanger O2 forms, in the three-effect absorption-type heat pump of solution series circulation; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, newly-increased solution pump 7, increase solution heat exchanger 8 newly, increase condenser 10 again and increase choke valve 11 again; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; There is the cryogen liquid pipeline in the 3rd choke valve L2 connection condenser D2 changes into, to press generator B2 to have the cryogen liquid pipeline to be communicated with middle pressure generator B2 and increases condenser 1 newly through the 3rd choke valve L2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser D2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator A2 again and increase condenser 10 again, increase condenser 10 again and also have the cryogen liquid pipeline to be communicated with newly-increased condenser 1, increase condenser 10 again and also have heated medium pipeline and external communications through increasing choke valve 11 again; Having the weak solution pipeline to be communicated with high pressure generator A2 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 absorber F2 again changes absorber F2 into and has the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with the 3rd solution heat exchanger O2 through solution pump G2, solution heat exchanger M2, the second solution heat exchanger N2 to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter 4 back through newly-increased solution heat exchanger 8 again to increase absorption-evaporimeter 4 newly and have weak solution pipeline warp to increase solution pump 7 newly again to be communicated with high pressure generator A2 with newly-increased solution heat exchanger 8; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Set up the cryogen liquid pipeline and be communicated with the newly-increased absorption-evaporimeter 4 in newly-increased absorptions-evaporimeter 4 back through newly-increased second choke valve 6 and have the refrigerant vapour pipeline connection to increase absorber 3 newly again by increasing condenser 10 again, increase absorber 3 heated medium pipeline and external communications in addition newly; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The heat supply that increases condenser 10 again derives from the refrigerant vapour of high pressure generator A2, is single-action flow process thermic load; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, can be regarded one generator two-stage flow process thermic load from absorber F2, refrigerant vapour as; Thereby obtain comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

The purpose that on the single-stage three-effect absorption-type heat pump basis of adopting solution parallel connection circulation, forms the quadruple composite absorption heat pump (type I) shown in Figure 19 is achieved in that

By high pressure generator A2, middle pressure generator B2, low pressure generator C2, condenser D2, evaporimeter E2, absorber F2, solution pump G2, choke valve J2, the second choke valve K2, the 3rd choke valve L2, solution heat exchanger M2, the second solution heat exchanger N2 and the 3rd solution heat exchanger O2 forms, in the three-effect absorption-type heat pump of solution parallel connection circulation; Increase newly-increased condenser 1, newly-increased choke valve 2, newly-increased absorber 3, newly-increased absorptions-evaporimeter 4, newly-increased second choke valve 6, newly-increased solution pump 7, newly-increased solution heat exchanger 8, increase second solution heat exchanger 9 newly, increase condenser 10 again and increase choke valve 11 again; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser D2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator A2 again and increase condenser 10 again, increase condenser 10 again and also have the cryogen liquid pipeline to be communicated with newly-increased condenser 1, increase condenser 10 again and also have heated medium pipeline and external communications through increasing choke valve 11 again; Set up the concentrated solution pipeline from high pressure generator A2 again and be communicated with newly-increased absorber 3 through newly-increased second solution heat exchanger 9; Newly-increased absorber 3 has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter 4 through newly-increased solution heat exchanger 8; Newly-increased absorption-evaporimeter 4 also has the weak solution pipeline to be communicated with high pressure generator A2 through newly-increased solution pump 7, newly-increased solution heat exchanger 8 with newly-increased second solution heat exchanger 9; Set up the cryogen liquid pipeline and be communicated with the newly-increased absorption-evaporimeter 4 in newly-increased absorptions-evaporimeter 4 back through newly-increased second choke valve 6 and have the refrigerant vapour pipeline connection to increase absorber 3 newly again by increasing condenser 10 again, increase absorber 3 heated medium pipeline and external communications in addition newly; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The heat supply that increases condenser 10 again derives from the refrigerant vapour of high pressure generator A2, is single-action flow process thermic load; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, can be regarded one generator two-stage flow process thermic load from high pressure generator A2, refrigerant vapour as; From obtaining the quadruple composite absorption heat pump (type I) that solution parallel connection circulation three-effect basis comprises triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

The purpose that on the single-stage three-effect absorption-type heat pump basis of adopting solution parallel connection circulation, forms the quadruple composite absorption heat pump (type I) shown in Figure 20 is achieved in that

By high pressure generator A2, middle pressure generator B2, low pressure generator C2, condenser D2, evaporimeter E2, absorber F2, solution pump G2, choke valve J2, the second choke valve K2, the 3rd choke valve L2, solution heat exchanger M2, the second solution heat exchanger N2 and the 3rd solution heat exchanger O2 forms, in the three-effect absorption-type heat pump of solution parallel connection circulation; Increase increases condenser 1 newly, increases choke valve 2 newly, increases absorber 3 newly, increases absorption-evaporimeter 4 newly, increases cryogen liquid pump 5 newly, increases solution pump 7 newly, increases solution heat exchanger 8 newly, increases condenser 10 again and increases choke valve 11 again; Set up the newly-increased condenser 1 of refrigerant vapour pipeline connection by middle pressure generator B2; Newly-increased condenser 1 also has the cryogen liquid pipeline to be communicated with condenser D2 through newly-increased choke valve 2, and newly-increased condenser 1 also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator A2 again and increase condenser 10 again, increase condenser 10 again and also have the cryogen liquid pipeline to be communicated with newly-increased condenser 1, increase condenser 10 again and also have heated medium pipeline and external communications through increasing choke valve 11 again; Having the weak solution pipeline to be communicated with high pressure generator A2 with solution heat exchanger M2 through solution pump G2 absorber F2 again changes absorber F2 into and has the weak solution pipeline to be communicated with newly-increased absorber 3, newly-increased absorber 3 with solution heat exchanger M2 through solution pump G2 to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter 4 back through newly-increased solution heat exchanger 8 again to increase absorption-evaporimeter 4 newly and have weak solution pipeline warp to increase solution pump 7 newly again to be communicated with high pressure generator A2 with newly-increased solution heat exchanger 8; Set up the newly-increased absorption-evaporimeter 4 of refrigerant vapour pipeline connection by evaporimeter E2; Setting up cryogen liquid pipeline newly-increased absorption-evaporimeter 4 after newly-increased cryogen liquid pump 5 is communicated with newly-increased absorption-evaporimeter 4 by evaporimeter E2 again has the refrigerant vapour pipeline connection to increase absorber 3 newly again, and newly-increased absorber 3 also has heated medium pipeline and external communications; Press the refrigerant vapour of generator B2 during the heat supply of newly-increased condenser 1 derives from, be the double-effect process thermic load; The heat supply that increases condenser 10 again derives from the refrigerant vapour of high pressure generator A2, is single-action flow process thermic load; The solution of newly-increased absorber 3 from waste heat supply temperature is promoted newly-increased absorption-evaporimeter 4 once, can be regarded one generator two-stage flow process thermic load from absorber F2, refrigerant vapour as; From obtaining the quadruple composite absorption heat pump (type I) that solution parallel connection circulation three-effect basis comprises triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

Shown in Figure 21, realize single-action, economic benefits and social benefits and triple effect mutual cooperate or the purpose of the multiple compound first class absorption heat pump of conversion is achieved in that

1. on the structure; In triple composite absorption heat pump (type I)s on solution series round-robin basis as shown in Figure 1, at condenser C1 and newly-increased condenser 1) between the heated medium pipeline on set up its bypass line, set up its branch line, increasing by the first control valve f1 on the heated medium pipeline, increasing by the second control valve f2 on the bypass line, setting up the 3rd control valve f3 on the branch line and on the heated medium pipeline between newly-increased condenser 1 and the newly-increased absorber 3, set up its bypass line, set up its branch line in newly-increased condenser 1 outlet in condenser C1 outlet, at increase the 5th control valve f5 on the heated medium pipeline, at increase the 6th control valve f6 on the bypass line, on newly-increased condensator outlet branch line, set up the 4th control valve f4.

2. on the flow process; The first control valve f1, the second control valve f2 close and the 3rd control valve f3 opens, when newly-increased choke valve 2 cuts out (like water seal); Newly-increased condenser 1 is not heated fluid and gets into; The refrigerant vapour of high pressure generator A1 can't condensation in newly-increased condenser 1, and unit moves according to double-effect process; The 5th control valve f5, the 6th control valve f6 close and the 4th control valve f4 when opening, and newly-increased cryogen liquid pump 5 is stopped transport, and unit is according to economic benefits and social benefits, the operation of single-action complex flow; When solution pump H1 stopped transport, economic benefits and social benefits and single-action flow process did not turn round, and unit is according to the two-stage process flow operation; Utilize unlatching between the different adjustment valve, close and different unlatching amplitudes, can realize cooperatively interacting between different flow processs, partly open the 6th control valve f6 like appropriateness, then the load proportion of two-stage flow process then can reduce.

Shown in Figure 21 is to realize conversion between different flow processs in the multiple compound first class absorption heat pump, a representative flow process that cooperates; Can obtain corresponding scalable multiple compound first class absorption heat pump in conjunction with concrete heat pump structure and flow process.

The effect that technology of the present invention can realize---multiple compound first class absorption heat pump proposed by the invention has following effect and advantage:

1. mainly increase the multiple compound first class absorption unit that formation such as condenser, absorption-evaporimeter, absorber, choke valve and solution pump comprise a plurality of flow processs, simple in structure.

2. integral type combined heat-pump flow process, be applied to heated medium temperature requirements wider range, the unit performance index is high when being fit to cross over different flow processs to the occasion of its heat supply, improves energy utilization rate.

3. can realize the conversion of multiple-effect, economic benefits and social benefits, single-action, two-stage flow process or cooperatively interact that dual-use or many usefulness are realizing the maximized as far as possible while of energy-saving benefit, improve utilization rate of equipment and installations.

4. can carry out the adjusting of unit load and heating parameter within the specific limits,, can give full play to related procedure advantage separately, improve energy-saving benefit in the occasion that is applied to load, the heat supply temperature excursion is bigger.

Claims

1. one of triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis; Be in the solution series circulation single-stage economic benefits and social benefits first kind absorption heat pump of forming by high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, second solution pump, solution heat exchanger and second solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by high pressure generator (A1); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (D1) or to have the cryogen liquid pipeline to be communicated with condenser (C1) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator (A1) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to be communicated with high pressure generator (A1) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) with newly-increased second solution heat exchanger (9); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (D1); Setting up the cryogen liquid pipeline by evaporimeter (D1) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by high pressure generator (A1); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (D1) or to have the cryogen liquid pipeline to be communicated with condenser (C1) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with low pressure generator (B1) with second solution heat exchanger (K1) through solution pump (H1), solution heat exchanger (J1) absorber (E1) again changes absorber (E1) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with second solution heat exchanger (K1) through solution pump (H1), solution heat exchanger (J1) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with low pressure generator (B1) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (D1); Setting up the cryogen liquid pipeline by evaporimeter (D1) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

2. two of the triple composite absorption heat pump (type I)s on the solution series circulation economic benefits and social benefits basis; Be in the solution series circulation single-stage economic benefits and social benefits first kind absorption heat pump of forming by high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, solution heat exchanger and second solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by high pressure generator (A1); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (D1) or to have the cryogen liquid pipeline to be communicated with condenser (C1) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator (A1) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to be communicated with high pressure generator (A1) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) with newly-increased second solution heat exchanger (9); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (D1); Setting up the cryogen liquid pipeline by evaporimeter (D1) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by high pressure generator (A1); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (D1) or to have the cryogen liquid pipeline to be communicated with condenser (C1) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator (A1) with second solution heat exchanger (K1) through solution pump (H1), solution heat exchanger (J1) absorber (E1) again changes absorber (E1) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with second solution heat exchanger (K1) through solution pump (H1), solution heat exchanger (J1) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with high pressure generator (A1) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (D1); Setting up the cryogen liquid pipeline by evaporimeter (D1) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

3. triple composite absorption heat pump (type I)s on the solution parallel connection circulation economic benefits and social benefits basis; Be in the solution parallel connection circulation single-stage economic benefits and social benefits first kind absorption heat pump of forming by high pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, solution pump, solution heat exchanger and second solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by high pressure generator (A1); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (D1) or to have the cryogen liquid pipeline to be communicated with condenser (C1) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from high pressure generator (A1) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to be communicated with high pressure generator (A1) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) with newly-increased second solution heat exchanger (9); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (D1); Setting up the cryogen liquid pipeline by evaporimeter (D1) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution parallel connection circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by high pressure generator (A1); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (D1) or to have the cryogen liquid pipeline to be communicated with condenser (C1) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator (A1) with solution heat exchanger (J1) through solution pump (H1) absorber (E1) again changes absorber (E1) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with solution heat exchanger (J1) through solution pump (H1) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with high pressure generator (A1) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (D1); Setting up the cryogen liquid pipeline by evaporimeter (D1) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution parallel connection circulation economic benefits and social benefits basis triple composite absorption heat pump (type I)s of double-effect process, single-action flow process and two-stage flow process.

4. one of triple composite absorption heat pump (type I)s on the solution series circulation three-effect basis; Be in the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, second solution pump, the 3rd solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator (B2) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to press generator (B2) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) and during newly-increased second solution heat exchanger (9) is communicated with; Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with low pressure generator (C2) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) absorber (F2) again changes absorber (F2) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with low pressure generator (C2) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process.

5. two of the triple composite absorption heat pump (type I)s on the solution series circulation three-effect basis; Be in the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator (B2) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to press generator (B2) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) and during newly-increased second solution heat exchanger (9) is communicated with; Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Having the weak solution pipeline to be communicated with high pressure generator (A2) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) absorber (F2) again changes absorber (F2) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with high pressure generator (A2) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process.

6. triple composite absorption heat pump (type I)s on the solution parallel connection circulation three-effect basis; Be in the solution parallel connection circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger and increase second solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the concentrated solution pipeline from middle pressure generator (B2) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to press generator (B2) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) and during newly-increased second solution heat exchanger (9) is communicated with; Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution parallel connection circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Again with absorber (F2) have the weak solution pipeline through solution pump (G2) with press during second solution heat exchanger (N2) is communicated with generator (B2) to change absorber (F2) into to have the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with second solution heat exchanger (N2) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again and press generator (B2) during newly-increased solution heat exchanger (8) is communicated with through newly-increased solution heat exchanger (8) through solution pump (G2); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline by newly-increased condenser (1) and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution parallel connection circulation three-effect basis triple composite absorption heat pump (type I)s of triple effect flow process, double-effect process and single-action flow process.

7. one of quadruple composite absorption heat pump (type I) on the solution series circulation three-effect basis; Be in the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, second solution pump, the 3rd solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger, increase second solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator (A2) again and increase condenser (10) again; Increase condenser (10) again or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) or newly-increased condenser (1), increase condenser (10) again and also have heated medium pipeline and external communications through increasing choke valve (11) again through increasing choke valve (11) again; Set up the concentrated solution pipeline from high pressure generator (A2) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to be communicated with high pressure generator (A2) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) with newly-increased second solution heat exchanger (9); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly by increasing condenser (10) again; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator (A2) again and increase condenser (10) again; Increase condenser (10) again or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) or newly-increased condenser (1), increase condenser (10) again and also have heated medium pipeline and external communications through increasing choke valve (11) again through increasing choke valve (11) again; Having the weak solution pipeline to be communicated with low pressure generator (C2) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) absorber (F2) again changes absorber (F2) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with low pressure generator (C2) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly by increasing condenser (10) again; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

8. two of the quadruple composite absorption heat pump (type I) on the solution series circulation three-effect basis; Be in the solution series circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger, increase second solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator (A2) again and increase condenser (10) again; Increase condenser (10) again or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) or newly-increased condenser (1), increase condenser (10) again and also have heated medium pipeline and external communications through increasing choke valve (11) again through increasing choke valve (11) again; Set up the concentrated solution pipeline from high pressure generator (A2) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to be communicated with high pressure generator (A2) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) with newly-increased second solution heat exchanger (9); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly by increasing condenser (10) again; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); There is the cryogen liquid pipeline in the 3rd choke valve (L2) connection condenser (D2) changes into, to press generator (B2) to have the cryogen liquid pipeline to be communicated with in middle pressure generator (B2) and increases condenser (1) newly through the 3rd choke valve (L2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator (A2) again and increase condenser (10) again; Increase condenser (10) again or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) or newly-increased condenser (1), increase condenser (10) again and also have heated medium pipeline and external communications through increasing choke valve (11) again through increasing choke valve (11) again; Having the weak solution pipeline to be communicated with high pressure generator (A2) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) absorber (F2) again changes absorber (F2) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with the 3rd solution heat exchanger (O2) through solution pump (G2), solution heat exchanger (M2), second solution heat exchanger (N2) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with high pressure generator (A2) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly by increasing condenser (10) again; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution series circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

9. the quadruple composite absorption heat pump (type I) on the solution parallel connection circulation three-effect basis; Be in the solution parallel connection circulation single-stage triple-effect first category absorption heat pump of forming by high pressure generator, middle pressure generator, low pressure generator, condenser, evaporimeter, absorber, choke valve, second choke valve, the 3rd choke valve, solution pump, solution heat exchanger, second solution heat exchanger and the 3rd solution heat exchanger; 1. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, newly-increased solution heat exchanger, increase second solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator (A2) again and increase condenser (10) again; Increase condenser (10) again or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) or newly-increased condenser (1), increase condenser (10) again and also have heated medium pipeline and external communications through increasing choke valve (11) again through increasing choke valve (11) again; Set up the concentrated solution pipeline from high pressure generator (A2) again and be communicated with newly-increased absorber (3) through newly-increased second solution heat exchanger (9); Newly-increased absorber (3) has the weak solution pipeline to be communicated with newly-increased absorption-evaporimeter (4) through newly-increased solution heat exchanger (8); Newly-increased absorption-evaporimeter (4) also has the weak solution pipeline to be communicated with high pressure generator (A2) through newly-increased solution pump (7), newly-increased solution heat exchanger (8) with newly-increased second solution heat exchanger (9); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly by increasing condenser (10) again; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution parallel connection circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process; 2. or increase newly-increased condenser, newly-increased choke valve, newly-increased absorber, newly-increased absorptions-evaporimeter, newly-increased cryogen liquid pump or newly-increased second choke valve, newly-increased solution pump, increase solution heat exchanger newly, increase condenser again and increase choke valve again; Set up the newly-increased condenser (1) of refrigerant vapour pipeline connection by middle pressure generator (B2); Increase condenser (1) newly or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) through increasing choke valve (2) newly through newly-increased choke valve (2), newly-increased condenser (1) also has heated medium pipeline and external communications; Set up the refrigerant vapour pipeline connection by high pressure generator (A2) again and increase condenser (10) again; Increase condenser (10) again or have the cryogen liquid pipeline to be communicated with evaporimeter (E2) or to have the cryogen liquid pipeline to be communicated with condenser (D2) or newly-increased condenser (1), increase condenser (10) again and also have heated medium pipeline and external communications through increasing choke valve (11) again through increasing choke valve (11) again; Having the weak solution pipeline to be communicated with high pressure generator (A2) with solution heat exchanger (M2) through solution pump (G2) absorber (F2) again changes absorber (F2) into and has the weak solution pipeline to be communicated with newly-increased absorber (3), newly-increased absorber (3) with solution heat exchanger (M2) through solution pump (G2) to have the weak solution pipeline to be communicated with newly-increased absorptions-evaporimeter (4) back through newly-increased solution heat exchanger (8) again to increase absorption-evaporimeter (4) newly and have weak solution pipeline warp to increase solution pump (7) newly again to be communicated with high pressure generator (A2) with newly-increased solution heat exchanger (8); Set up the newly-increased absorption-evaporimeter (4) of refrigerant vapour pipeline connection by evaporimeter (E2); Setting up the cryogen liquid pipeline by evaporimeter (E2) is communicated with the newly-increased absorptions-evaporimeter (4) in newly-increased absorptions-evaporimeter (4) back through newly-increased cryogen liquid pump (5) and has the refrigerant vapour pipeline connection increase absorber (3) again or set up the cryogen liquid pipeline and increase absorption-evaporimeter (4) newly after second choke valve (6) connection increases absorption-evaporimeter (4) newly and have the refrigerant vapour pipeline connection to increase absorber (3) newly again through increasing newly by increasing condenser (10) again; Newly-increased absorber (3) also has heated medium pipeline and external communications, obtains comprising on the solution parallel connection circulation three-effect basis quadruple composite absorption heat pump (type I) of triple effect flow process, double-effect process, single-action flow process and two-stage flow process.

10. in the triple composite absorption heat pump (type I)s on the said economic benefits and social benefits of claim 1-claim 3 basis; Increase heated medium branch line and bypass line; And on heated medium pipeline and bypass line, increase by first control valve (f1), second control valve (f2), the 3rd control valve (f3), the 4th control valve (f4), the 5th control valve (f5) and the 6th control valve (f6); Setting up its bypass line on the heated medium pipeline between condenser (C1) and the newly-increased condenser (1), set up its branch line in condenser (C1) outlet, increasing by first control valve (f1) on the heated medium pipeline, increasing by second control valve (f2) on the bypass line, setting up the 3rd control valve (f3) on the branch line and on the heated medium pipeline between newly-increased condenser (1) and the newly-increased absorber (3), setting up its bypass line, setting up its branch line, increasing the 5th control valve (f5) on the heated medium pipeline, exporting on the branch line at increase the 6th control valve (f6) on the bypass line, at newly-increased condenser (1) and set up the 4th control valve (f4) in newly-increased condenser (1) outlet, accomplished single-action, economic benefits and social benefits and triple effect are mutual cooperates or triple composite absorption heat pump (type I)s of conversion.