CN106403359B

CN106403359B - Class thermally driven compression-absorption heat pump

Info

Publication number: CN106403359B
Application number: CN201610813859.3A
Authority: CN
Inventors: 李华玉
Original assignee: Individual
Current assignee: Individual
Priority date: 2015-12-30
Filing date: 2016-08-30
Publication date: 2020-01-31
Anticipated expiration: 2036-08-30
Also published as: CN106403359A

Abstract

The invention provides a -class heat-driven compression-absorption heat pump, which belongs to the technical field of power, refrigeration and heat pumps and comprises a front-end temperature difference utilization system consisting of an evaporator, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger, and a tail-end temperature difference utilization system consisting of an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump and a solution heat exchanger, wherein the front-end temperature difference utilization system acquires external low-temperature heat load and provides medium-temperature heat demand for the evaporator, the tail-end temperature difference utilization system acquires the heat load of the evaporator, and the absorber and the condenser provide the medium-temperature heat load to form the -class heat-driven compression-absorption heat pump.

Description

Class thermally driven compression-absorption heat pump

The technical field is as follows:

the invention belongs to the technical field of power, refrigeration and heat pumps.

Background art:

cold demand, heat demand and power demand, which are common in human life and production; in reality, people often need to use high-temperature heat energy to realize refrigeration, heat supply or power conversion, and also need to use power to refrigerate or use power and combine low-temperature heat energy to supply heat. In the process of achieving the above purpose, various condition limitations are faced, such as the type, grade and quantity of energy, the type, grade and quantity of user requirements, the type of working medium, the flow, structure and manufacturing cost of equipment, the safety of equipment operation, the acceptable degree of environmental temperature and environment, and the like.

A heat energy (temperature difference) utilization technology represented by an absorption heat pump technology, and high-temperature heat load driving is utilized to realize heat supply or refrigeration; due to the influence of the properties of the working medium (solution and refrigerant medium), the high-temperature heat load with too high temperature or the low-temperature heat load with too low temperature is difficult to be reasonably applied to the absorption heat pump technology, so that the application field and the application range of the absorption heat pump technology are greatly limited. The compression heat pump technology has better flexibility in thermodynamic performance, but the core component of the compression heat pump is a moving component, which brings many disadvantages, such as that noise generated in the operation of the compression heat pump is intolerable, and the core component cost is limited; for this reason, it is considered to reduce the use and number of core moving parts (compressor and expander).

In order to exert the respective technical advantages of a compression heat pump and an absorption heat pump, and aim at utilizing fuel as a driving energy source for supplying heat or cold and considering power drive or external power supply requirements, the invention provides an -class heat-driven compression-absorption heat pump which is characterized in that a front-end temperature difference utilization system is formed by taking a compressor and a gas turbine as core components, a tail-end temperature difference utilization system is formed by an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump and a solution heat exchanger, and fuel gas is used as a working medium and a heat source medium.

The invention content is as follows:

the invention mainly aims to provide a series type heat-driven compression-absorption heat pump, and the specific contents are explained in different terms as follows:

1. the type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supply device and a low-temperature heat exchanger, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber, the combustion chamber is also provided with a fuel channel communicated with the outside, the combustion chamber is also provided with the gas turbine, the gas turbine is also provided with the second gas turbine through the evaporator, the second gas turbine is also provided with the gas channel communicated with the third compressor through the heat exchanger, the third compressor is also provided with the gas turbine, the heat supply device, the heat exchanger, the generator is also provided with the second gas turbine, the heat supply device, the heat pump, the heat supply device is also communicated with the second compressor, the heat pump, the heat exchanger, the heat supply device is also provided with the second compressor, the heat exchanger, the.

2. class heat-driven compression-absorption heat pump mainly comprises absorber, generator, condenser, evaporator, throttle valve, solution pump, solution heat exchanger, compressor, combustion chamber, gas turbine, second compressor, second gas turbine, third compressor, heat supplier and low temperature heat exchanger, wherein the absorber has dilute solution pipeline connected to the generator via solution pump and solution heat exchanger, the generator also has concentrated solution pipeline connected to the absorber via solution heat exchanger, the generator also has refrigerant steam channel connected to the condenser, the condenser also has refrigerant steam channel connected to the evaporator via throttle valve, the evaporator also has refrigerant steam channel connected to the absorber, the external air channel is connected to the compressor, the compressor also has compressed air channel connected to the combustion chamber, the combustion chamber also has fuel channel connected to the external, the combustion chamber also has gas channel connected to the gas turbine, the gas turbine also has gas channel connected to the third compressor via low temperature heat exchanger, the third compressor also has gas channel connected to the second gas turbine via heat supplier, the second gas turbine also has fuel channel connected to the second compressor via evaporator, the second compressor also has heat supplier connected to the generator, the third compressor via low temperature heat exchanger, the heat compressor and the second compressor class heat exchanger, the second compressor also has heat-driven compressor connected to the second compressor and the heat exchanger, the heat compressor, the second compressor and the heat supplier.

3. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a third compressor, a heat supply device, a low-temperature heat exchanger and a fourth compressor, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, a refrigerant steam channel is communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber, the combustion chamber is also provided with a fuel channel communicated with the external, the combustion chamber is also provided with the gas turbine, the gas turbine is also provided with the gas channel communicated with the third compressor through the low-temperature heat exchanger, the third compressor is also provided with the gas channel communicated with the fourth compressor through the evaporator, the fourth compressor is also provided with a gas channel communicated with the second compressor through the heat supply device, the generator, the heat exchanger, the fourth compressor is also provided with the heat exchanger, the heat supply device, the fourth compressor, the heat exchanger is also provided with the fourth compressor, the heat exchanger.

4. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a heat supply device, a low-temperature heat exchanger and a third gas turbine, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber, the combustion chamber is also provided with a fuel channel communicated with the outside, the combustion chamber is also provided with the gas turbine, the gas turbine is also provided with the second gas turbine through the heat supply device, the second gas turbine is also provided with the gas turbine, the third gas turbine is also provided with the gas turbine, the heat exchanger is also provided with the heat supply device, the second gas turbine, the heat exchanger, the second gas turbine is communicated with.

5. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, a refrigerant steam channel is communicated with the condenser, the condenser is also provided with a refrigerant steam pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber, the combustion chamber is also provided with a fuel channel communicated with the outside, the combustion chamber is also provided with the gas turbine, the gas turbine is also provided with the third compressor through the evaporator, the third compressor is also provided with a gas channel communicated with the second gas turbine through the heat exchanger, the second gas turbine is also provided with the generator, the heat supplier is also provided with the heat exchanger, the second compressor, the heat supplier is also communicated with the second compressor, the heat exchanger, the heat-driven compressor, the generator is also provided with the heat supplier, the second compressor, the heat supplier is also provided with the heat exchanger, the heat supplier, the third compressor and the heat exchanger.

6. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber through the high-temperature heat regenerator, the combustion chamber is also provided with the external through a fuel channel, the combustion chamber is also provided with the gas turbine and the gas turbine, the gas turbine is also provided with a gas turbine, the gas turbine is also provided with the third gas turbine, the gas turbine is also provided with a gas turbine, the gas turbine is also provided with the heat exchanger, the gas turbine is also provided with the third compressor, the gas turbine, the gas.

7. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber through the high-temperature heat regenerator, the combustion chamber is also provided with the external through a fuel channel, the combustion chamber is also provided with the gas turbine and the gas turbine, the gas turbine is also provided with a gas channel communicated with the second gas turbine and the second gas turbine through the high-temperature heat exchanger, the second gas turbine is also provided with a gas turbine, the heat exchanger, the third compressor is also provided with a heat-driven compression heat exchanger, the third compressor, the gas turbine is also provided with a heat exchanger, the gas turbine is also provided with a heat exchanger, the gas turbine, the third gas turbine, the gas turbine is also provided with the third gas turbine, the.

8. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a fourth compressor and a high-temperature heat regenerator, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber through the high-temperature heat regenerator, the combustion chamber is also provided with the fuel channel communicated with the external, the combustion chamber is also provided with the gas turbine, the gas turbine is also provided with a gas channel communicated with the second gas turbine and the second gas turbine through the high-temperature heat exchanger, the second gas turbine is also provided with a gas compressor , the second compressor, the heat compressor is also provided with the heat exchanger, the heat compressor, the third gas turbine is also provided with the heat exchanger, the fourth gas turbine, the heat compressor is also provided with the fourth gas turbine, the heat compressor, the second compressor, the heat compressor.

9. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a heat supply device, a low-temperature heat exchanger, a third gas turbine, a high-temperature heat regenerator and a fourth gas turbine, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber through the high-temperature heat regenerator, the combustion chamber is also provided with a fuel channel communicated with the external, the combustion chamber is also provided with the gas turbine and a gas turbine, the gas turbine is also provided with a gas channel communicated with the second gas turbine, the second gas turbine is also provided with a gas turbine, a fourth gas turbine, a gas turbine is also provided with a heat exchanger, a gas turbine is also provided with a fourth gas turbine, a fourth gas turbine, a heat transfer channel communicated with a fourth gas turbine, a heat exchanger, a fourth gas turbine, a heat exchanger.

10. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator, wherein the absorber is provided with a dilute solution pipeline communicated with the generator through the solution pump and the solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through the throttle valve, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, an external air channel is communicated with the compressor, the compressor is also provided with a compressed air channel communicated with the combustion chamber through the high-temperature heat regenerator, the combustion chamber is also provided with the external through a fuel channel, the combustion chamber is also provided with the gas turbine and the gas turbine, the gas turbine is also provided with a gas channel communicated with the second gas turbine through the high-temperature heat regenerator, the second gas turbine is also provided with a gas turbine, the third compressor, the gas turbine is also provided with a heat exchanger, the gas turbine is also provided with a gas turbine, the third compressor, the gas turbine is also provided with a gas turbine, the gas turbine is also provided with the gas turbine, the third gas turbine.

11. An th class heat-driven compression-absorption heat pump, which is a th class heat-driven compression-absorption heat pump, in any th class heat-driven compression-absorption heat pump described in items 1-10, a fuel channel communicated with a combustion chamber is eliminated, a newly added compressor is added, a gaseous fuel channel is arranged outside and communicated with the newly added compressor, the newly added compressor is also communicated with the combustion chamber, and a gas turbine is connected with the newly added compressor and transmits power to form the th class heat-driven compression-absorption heat pump.

12. An th class heat-driven compression-absorption heat pump, which is characterized in that a second heat supply device is added in the th class heat-driven compression-absorption heat pump in items 1-11, a fuel gas channel of a second compressor is communicated with the outside through a generator and adjusted to be communicated with the generator and the second heat supply device in sequence, then the fuel gas channel of the second heat supply device is communicated with the outside, and a heated medium channel of the second heat supply device is communicated with the outside to form the class heat-driven compression-absorption heat pump.

13. An th class heat-driven compression-absorption heat pump, which is characterized in that a second heat supply device is added in the th class heat-driven compression-absorption heat pump in items 1-11, a fuel gas channel of a second compressor is communicated with the outside through a generator and adjusted to be communicated with the generator, the second heat supply device and an evaporator in sequence, then the fuel gas channel of the evaporator is communicated with the outside, and a heated medium channel of the second heat supply device is communicated with the outside to form the class heat-driven compression-absorption heat pump.

14. An th class heat-driven compression-absorption heat pump, which is characterized in that a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added in any th class heat-driven compression-absorption heat pump in items 1-11, a dilute solution pipeline is additionally arranged on an absorber and is communicated with the second generator through the second solution pump and the second solution heat exchanger, a concentrated solution pipeline is also communicated with the absorber through the second solution heat exchanger, a refrigerant steam channel of the generator is communicated with a condenser, the refrigerant steam channel of the second generator is adjusted to be communicated with the second generator, then the refrigerant liquid pipeline of the second generator is communicated with the condenser through the second throttle valve, and the refrigerant steam channel of the second generator is communicated with the condenser to form a th class heat-driven compression-absorption heat pump.

15. An th class heat-driven compression-absorption heat pump, which is prepared by adding a second generator, a second throttle valve and a second solution heat exchanger in any th class heat-driven compression-absorption heat pump described in items 1-11, adjusting the connection of an absorber with a dilute solution pipeline through a solution pump and a solution heat exchanger to the generator, adjusting the connection of an absorber with a dilute solution pipeline through a solution pump, a solution heat exchanger and a second solution heat exchanger to the generator, adjusting the connection of a generator with a concentrated solution pipeline through a solution heat exchanger to the absorber, adjusting the connection of a generator with a concentrated solution pipeline through a solution heat exchanger to the generator, connecting the generator with a second generator with a concentrated solution pipeline through a second solution heat exchanger to the second generator, connecting the generator with a condenser through a refrigerant vapor channel, connecting the second generator with a refrigerant liquid pipeline through a second throttle valve to the condenser, and connecting the second generator with a refrigerant vapor channel to the condenser to form a th class heat-driven compression-absorption heat pump.

16. An th class heat-driven compression-absorption heat pump, which is prepared by adding a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger in any th class heat-driven compression-absorption heat pump described in items 1-11, adjusting the connection of an absorber with a dilute solution pipeline through the solution pump and the solution heat exchanger to the generator, adjusting the connection of an absorber with a dilute solution pipeline through the solution pump and the solution heat exchanger to the second generator, adjusting the connection of a generator with a concentrated solution pipeline through the solution heat exchanger to the absorber, adjusting the connection of a generator with a concentrated solution pipeline through the second solution heat exchanger and the solution heat exchanger to the absorber, adjusting the connection of a generator with a refrigerant vapor channel to the condenser to the connection of a generator with a refrigerant vapor channel to the second generator, then connecting the second generator with a refrigerant liquid pipeline through the second throttle valve to the condenser, and connecting the second generator with a refrigerant vapor channel to the condenser to form a th class heat-driven compression-absorption heat pump.

17. An th class heat-driven compression-absorption heat pump, which is characterized in that a second heat supply device is added in the th class heat-driven compression-absorption heat pump in 14-16 th items, a fuel gas channel of a second compressor is communicated with the outside through a generator and adjusted to be communicated with the generator and the second heat supply device in sequence, then the fuel gas channel of the second compressor is communicated with the outside, and a heated medium channel of the second heat supply device is communicated with the outside to form the th class heat-driven compression-absorption heat pump.

18. An th class heat-driven compression-absorption heat pump, which is characterized in that a second heat supply device is added in the th class heat-driven compression-absorption heat pump in 14-16 th items, a fuel gas channel of a second compressor is communicated with the outside through a generator and adjusted to be communicated with the generator, the second heat supply device and an evaporator in sequence, then the fuel gas channel of the evaporator is communicated with the outside, and a heated medium channel of the second heat supply device is communicated with the outside to form the class heat-driven compression-absorption heat pump.

19. An th class heat-driven compression-absorption heat pump, which is the th th class heat-driven compression-absorption heat pump described in 14-16 th items, wherein the second compressor is provided with a fuel gas channel which is communicated with the outside through a generator, and the second compressor is provided with a fuel gas channel which is communicated with the generator and the second generator in turn, and then the second generator is provided with a fuel gas channel which is communicated with the outside, so that the th class heat-driven compression-absorption heat pump is formed.

20. An th class heat-driven compression-absorption heat pump, which is characterized in that a second heat supply device is added in the th class heat-driven compression-absorption heat pump in 14-16 th items, a fuel gas channel of a second compressor is communicated with the outside through a generator and adjusted to be communicated with the generator, the second generator and the second heat supply device in sequence, then the fuel gas channel of the second heat supply device is communicated with the outside, and a heated medium channel of the second heat supply device is communicated with the outside to form the class heat-driven compression-absorption heat pump.

21. An th class heat-driven compression-absorption heat pump, which is characterized in that a second heat supply device is added in the th class heat-driven compression-absorption heat pump in 14-16 th items, a fuel gas channel of a second compressor is communicated with the outside through a generator and adjusted to be communicated with the generator, the second heat supply device and an evaporator in sequence, then the evaporator is further provided with a fuel gas channel and the outside, and the second heat supply device is further provided with a heated medium channel and is communicated with the outside to form the th class heat-driven compression-absorption heat pump.

22. An th class heat-driven compression-absorption heat pump, which is characterized in that a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added in any th class heat-driven compression-absorption heat pump in items 1-11, wherein the evaporator is provided with a refrigerant steam channel communicated with the absorber and adjusted to be communicated with the second absorber, the second absorber is also provided with a dilute solution pipeline communicated with the second generator through the second solution pump and the second solution heat exchanger, the second generator is also provided with a concentrated solution pipeline communicated with the second absorber through the second solution heat exchanger, the second generator is also provided with a refrigerant steam channel communicated with the absorber, the second compressor is provided with a fuel gas channel communicated with the outside through the generator channel and adjusted to be communicated with the generator and the second generator in sequence, then the second generator is further provided with a fuel gas channel communicated with the outside, and the second absorber is also provided with a heated medium channel communicated with the outside to form the th class heat-driven compression-absorption heat pump.

23. A class heat-driven compression-absorption heat pump is characterized in that a second generator, a second absorber, a second solution pump, a solution throttle valve, a second solution throttle valve and a steam distribution chamber are added in any class heat-driven compression-absorption heat pump in items 1-11, the absorber is provided with a dilute solution pipeline which is communicated with the generator through the solution pump and the solution heat exchanger and is adjusted to be provided with a dilute solution pipeline which is communicated with the second absorber through the solution pump and the solution heat exchanger, the second absorber is also provided with a dilute solution pipeline which is communicated with the second generator through the solution throttle valve, the second generator is further provided with a concentrated solution pipeline which is communicated with the generator through the second solution pump, the generator is provided with a concentrated solution pipeline which is adjusted to be communicated with the absorber through the solution heat exchanger, the absorber is further provided with a concentrated solution pipeline which is communicated with the absorber through the solution heat exchanger, the generator is provided with a refrigerant steam channel which is adjusted to be provided with the generator through the refrigerant steam channel which is communicated with the second generator, the second generator and the steam distribution chamber are also provided with a fuel gas compressor which are sequentially communicated with the second generator through the gas compressor .

24. An th class heat-driven compression-absorption heat pump, which is a th class heat-driven compression-absorption heat pump driven by additional external power, wherein a power machine is added in the th class heat-driven compression-absorption heat pump from item 1 to item 23, and the power machine is connected with and transmits power to a second compressor.

25. The th class heat-driven compression-absorption heat pump is a th class heat-driven compression-absorption heat pump which is additionally provided with a working machine in any th class heat-driven compression-absorption heat pump from items 1 to 23, wherein a gas turbine is connected with the working machine and transmits power to the working machine to form an additional power load externally provided.

Description of the drawings:

figure 1 is a schematic thermodynamic system diagram of class heat driven compression-absorption heat pump type 1 according to the present invention.

Figure 2 is a schematic thermodynamic system diagram of class heat driven compression-absorption heat pump type 2 in accordance with the present invention.

Figure 3 is a schematic thermodynamic system diagram of class heat driven compression-absorption heat pump type 3 according to the present invention.

Figure 4 is a diagram of a 4 th principle thermodynamic system for a class thermally driven compression-absorption heat pump according to the present invention.

Figure 5 is a diagram of a class thermally driven compression-absorption heat pump, category 5 principle thermodynamic system provided in accordance with the present invention.

Figure 6 is a schematic thermodynamic system diagram of class heat driven compression-absorption heat pump type 6 in accordance with the present invention.

Figure 7 is a 7 th principle thermodynamic system diagram of a class thermally driven compression-absorption heat pump according to the present invention.

Figure 8 is a diagram of a 8 th principle thermodynamic system for a class thermally driven compression-absorption heat pump according to the present invention.

Figure 9 is a diagram of a class thermally driven compression-absorption heat pump type 9 principle thermodynamic system provided in accordance with the present invention.

Figure 10 is a 10 th principle thermodynamic system diagram of a class thermally driven compression-absorption heat pump according to the present invention.

Figure 11 is a diagram of the 11 th principle thermodynamic system of a class thermally driven compression-absorption heat pump according to the present invention.

Figure 12 is a schematic thermodynamic system diagram of class heat driven compression-absorption heat pump type 12 in accordance with the present invention.

Figure 13 is a 13 th principle thermodynamic system diagram of a class thermally driven compression-absorption heat pump according to the present invention.

Figure 14 is a diagram of a 14 th principle thermodynamic system for a class thermally driven compression-absorption heat pump according to the present invention.

Figure 15 is a diagram of a 15 th principle thermodynamic system for a class thermally driven compression-absorption heat pump according to the present invention.

Figure 16 is a diagram of a 16 th principle thermodynamic system for a class thermally driven compression-absorption heat pump according to the present invention.

Figure 17 is a diagram of a 17 th principle thermodynamic system for a class thermally driven compression-absorption heat pump according to the present invention.

Figure 18 is a diagram of the 18 th principle thermodynamic system of a class thermally driven compression-absorption heat pump according to the present invention.

In the figure, 1-absorber, 2-generator, 3-condenser, 4-evaporator, 5-throttle, 6-solution pump, 7-solution heat exchanger, 8-compressor, 9-combustion chamber, 10-gas turbine, 11-second compressor, 12-second gas turbine, 13-third compressor, 14-heater, 15-low temperature heat exchanger, 16-fourth compressor, 17-third gas turbine, 18-high temperature regenerator, 19-fourth gas turbine, 20-fresh compressor, 21-second heater, 22-second generator, 23-second throttle, 24-second solution pump, 25-second solution heat exchanger, 26-second absorber, 27-solution throttle, 28-second solution throttle valve, 29-steam separation chamber.

The specific implementation mode is as follows:

it is to be noted that, in the description of the structure and the flow, the repetition is not necessary; obvious flow is not described. The invention is described in detail below with reference to the figures and examples.

The -th class thermally driven compression-absorption heat pump shown in fig. 1 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with the condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with the evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with the compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with the combustion chamber 9, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with the gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with the second gas turbine 12 through the evaporator 4, the second gas turbine 12 is also provided with a fuel gas channel which, the second compressor 11 also has a gas channel communicated with the outside through the generator 2, the absorber 1, the condenser 3 and the heater 14 also have heated medium pipelines communicated with the outside respectively, the low-temperature heat exchanger 15 also has a low-temperature heat medium channel communicated with the outside, and the gas turbine 10 and the second gas turbine 12 are connected with the compressor 8, the second compressor 11 and the third compressor 13 and transmit power.

(2) In the process, dilute solution of an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, the heated solution enters the generator 1 to release refrigerant steam and is provided for a condenser 3, concentrated solution of the generator 2 enters the absorber 1 through the solution heat exchanger 7 to absorb the refrigerant steam and release heat to a heated medium, the refrigerant steam of the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid of the condenser 3 is throttled through a throttle valve 5 to enter an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, compressed air discharged by the compressor 8 enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with the compressed air and is burnt to form high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and made work, fuel gas discharged by the gas turbine 10 flows through the evaporator 4 to release heat and then enters a second gas turbine 12 to be decompressed and made work, fuel gas discharged by the second gas turbine 12 flows through a low-temperature heat exchanger 15 to enter a third compressor 13 to be boosted, the second gas turbine 13 to discharge heat compressor 358 to form heat and heat compressor 13 to discharge and to form second heat compressor 13 to discharge power and compressor 3511 to discharge and compressor 13 to discharge the second compressor 13 to discharge heat compressor 13 to discharge the second compressor 11 and to discharge the second compressor 11 to.

The -th class thermally driven compression-absorption heat pump shown in fig. 2 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with the condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with the evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a third compressor 13 through a low-temperature heat exchanger 15, the third compressor 13 is also provided with a fuel gas channel, the second compressor 11 also has a gas channel communicated with the outside through the generator 2, the absorber 1, the condenser 3 and the heater 14 also have heated medium pipelines communicated with the outside respectively, the low-temperature heat exchanger 15 also has a low-temperature heat medium channel communicated with the outside, and the gas turbine 10 and the second gas turbine 12 are connected with the compressor 8, the second compressor 11 and the third compressor 13 and transmit power.

(2) In the process, dilute solution in an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, the heated solution enters the generator 1 to release refrigerant steam and is provided for a condenser 3, concentrated solution in the generator 2 enters the absorber 1 through the solution heat exchanger 7 to absorb the refrigerant steam and release heat to a heated medium, the refrigerant steam in the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid in the condenser 3 is throttled through a throttle valve 5 to enter an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, compressed air discharged by the compressor 8 enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with the compressed air and is burnt to form high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and work, fuel gas discharged by the gas turbine 10 flows through a low-temperature heat exchanger 15 to absorb heat and then enters a third compressor 13 to be boosted and heated, the fuel gas discharged by the third compressor 13 to flow through a second gas turbine 14 to release heat and then enters a second gas turbine 12 to be decompressed and heated to form heat compressor 358 and heat compressor 13 to be discharged to form heat and heat compressor 3511 and heat compressor and to be supplied to the second gas turbine 12 and to be discharged by the second heat compressor 12 and the second heat compressor 3511 to be discharged to form the second heat compressor.

The -th class thermally driven compression-absorption heat pump shown in fig. 3 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a third compressor, a heat supplier, a low-temperature heat exchanger and a fourth compressor; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with a condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with an evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a third compressor 13 through a low-temperature heat exchanger 15, the third compressor 13 is also provided with a, the second compressor 11 is also provided with a gas channel which is communicated with the outside through the generator 2, the absorber 1, the condenser 3 and the heat supplier 14 are also respectively provided with a heated medium pipeline which is communicated with the outside, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10 is connected with the compressor 8, the second compressor 11, the third compressor 13 and the fourth compressor 16 and transmits power.

(2) In the process, dilute solution of an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, the heated solution enters the generator 1 to release refrigerant steam and is provided for a condenser 3, concentrated solution of the generator 2 enters the absorber 1 through the solution heat exchanger 7 to absorb the refrigerant steam and release heat to a heated medium, the refrigerant steam of the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid of the condenser 3 is throttled through a throttle valve 5 to enter an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, compressed air discharged by the compressor 8 enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with the compressed air and is burnt to form high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to perform depressurization and work, the fuel gas discharged by the gas turbine 10 flows through a low-temperature heat exchanger 15 to absorb heat and then enters a third compressor 13 to be boosted and heated, the fuel gas discharged by the evaporator 4 to enter a fourth compressor 16 to be boosted, the fourth compressor 16 to perform heat release and heat emission by a heat compressor 358 to form heat and a heat absorption compressor 358 and a heat compressor 16 to output power compressor.

The -th class thermally driven compression-absorption heat pump shown in fig. 4 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a heat supplier, a low-temperature heat exchanger and a third gas turbine; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with the condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with the evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a second gas turbine 12 through a heat supply device 14, the second gas turbine 12 is also provided with a fuel gas channel which is, the second compressor 11 is also provided with a gas channel which is communicated with the outside through the generator 2, the absorber 1, the condenser 3 and the heat supplier 14 are also respectively provided with a heated medium pipeline which is communicated with the outside, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10, the second gas turbine 12 and the third gas turbine 17 are connected with the compressor 8 and the second compressor 11 and transmit power.

(2) In the process, dilute solution of an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, the heated solution enters the generator to release refrigerant steam and is provided for a condenser 3, concentrated solution of the generator 2 enters the absorber 1 through the solution heat exchanger 7, the refrigerant steam absorbs the refrigerant steam and releases heat to a heated medium, the refrigerant steam of the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid of the condenser 3 is throttled through a throttle valve 5 and enters an evaporator 4 to absorb heat to form refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, compressed air discharged by the compressor 8 enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with the compressed air and is burnt to form high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and made work, fuel gas discharged by the gas turbine 10 flows through a heat supply device 14 to release heat and then enters a second gas turbine 12 to be decompressed and made work, fuel gas discharged by the evaporator 4 to enter a third gas turbine 17 to be decompressed and made work, fuel gas turbine 17 flows through a low-temperature heat supply device 15 and a second heat supply device 11 to the second gas turbine 11 to drive the second gas turbine 10 to discharge compressor 358 and the second gas turbine 10 to discharge heat compressor 11 to discharge heat absorption compressor 11 to form heat absorption compressor 358 to discharge and to form heat absorption compressor 10 to.

The -th class thermally driven compression-absorption heat pump shown in fig. 5 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with the condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with the evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a third compressor 13 through the evaporator 4, the third compressor 13 is also provided with a fuel gas channel which is communicated, the second compressor 11 also has a gas channel communicated with the outside through the generator 2, the absorber 1, the condenser 3 and the heater 14 also have heated medium pipelines communicated with the outside respectively, the low-temperature heat exchanger 15 also has a low-temperature heat medium channel communicated with the outside, and the gas turbine 10 and the second gas turbine 12 are connected with the compressor 8, the second compressor 11 and the third compressor 13 and transmit power.

(2) In the process, dilute solution in an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, the heated solution enters the generator 1 to release refrigerant steam and is provided for a condenser 3, concentrated solution in the generator 2 enters the absorber 1 through the solution heat exchanger 7 to absorb the refrigerant steam and release heat to a heated medium, the refrigerant steam in the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid in the condenser 3 is throttled through a throttle valve 5 to enter an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, compressed air discharged by the compressor 8 enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with the compressed air and is burnt to form high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and work, fuel gas discharged by the gas turbine 10 flows through the evaporator 4 to release heat and then enters a third compressor 13 to be boosted and heated, fuel gas discharged by the third compressor 13 flows through a second gas turbine 14 to release heat and then enters a second gas turbine 12 to be decompressed and worked, the second gas turbine 12 to discharge heat exchanger 15 to form heat exchanger 3511 and heat compressor 13 to discharge heat and to discharge the second heat compressor 358 and to discharge heat compressor 11 and to form heat compressor 13 to discharge heat to discharge the second heat compressor and to discharge the second heat compressor 358 to discharge heat.

The -th class thermally driven compression-absorption heat pump shown in fig. 6 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with a condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with an evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9 through a high-temperature regenerator 18, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a second gas turbine 12 through the high, the third gas turbine 17 is also provided with a gas channel which is communicated with the third compressor 13 through a low-temperature heat exchanger 15, the third compressor 13 is also provided with a gas channel which is communicated with the second compressor 11 through a heat supplier 14, the second compressor 11 is also provided with a gas channel which is communicated with the outside through a generator 2, the absorber 1, the condenser 3 and the heat supplier 14 are also respectively communicated with the outside through heated medium pipelines, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10, the second gas turbine 12 and the third gas turbine 17 are connected with the compressor 8, the second compressor 11 and the third compressor 13 and transmit power.

(2) In the process, dilute solution of an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, heats the solution entering the generator to release refrigerant steam and is provided for a condenser 3, concentrated solution of the generator 2 enters the absorber 1 through the solution heat exchanger 7, absorbs the refrigerant steam and releases heat to a heated medium, the refrigerant steam of the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid of the condenser 3 is throttled by a throttle valve 5 and enters an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, flows through a high-temperature regenerator 18 to absorb heat and then enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with compressed air and is combusted into high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and powered, the fuel gas discharged from the gas turbine 10 flows through the high-temperature regenerator 18 to release heat and then enters a second gas turbine 12 to be decompressed, the fuel gas discharged from the second gas turbine 12 flows through the evaporator 4 to be decompressed and then enters a third gas turbine 17 to be powered, the third gas turbine 17 to be decompressed and discharged from a third gas turbine 17 to be heated, flows through a third heat exchanger 15 to be heated, flows through a third gas turbine 13 to be heated, and is discharged from the third gas turbine 11 to be heated and is discharged to form a third gas turbine 13 to be heated and is discharged to be heated, and is.

The -th class thermally driven compression-absorption heat pump shown in fig. 7 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with a condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with an evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9 through a high-temperature regenerator 18, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a second gas turbine 12 through, the third compressor 13 is also provided with a gas channel which is communicated with a third gas turbine 17 through a heat supply device 14, the third gas turbine 17 is also provided with a gas channel which is communicated with the second compressor 11 through an evaporator 4, the second compressor 11 is also provided with a gas channel which is communicated with the outside through a generator 2, the absorber 1, the condenser 3 and the heat supply device 14 are also respectively provided with a heated medium pipeline which is communicated with the outside, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10, the second gas turbine 12 and the third gas turbine 17 are connected with the compressor 8, the second compressor 11 and the third compressor 13 and transmit power.

(2) In the process, dilute solution in an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, heats the solution entering the generator to release refrigerant steam and is provided for a condenser 3, concentrated solution in the generator 2 enters the absorber 1 through the solution heat exchanger 7, absorbs the refrigerant steam and releases heat to a heated medium, the refrigerant steam in the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid in the condenser 3 is throttled by a throttle valve 5 and enters an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, flows through a high-temperature regenerator 18 to absorb heat and then enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with compressed air and is combusted into high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and does work, the fuel gas discharged from the gas turbine 10 flows through the high-temperature regenerator 18 to release heat and then enters a second gas turbine 12 to be decompressed, the fuel gas discharged from the second gas turbine 12 flows through a low-temperature heat exchanger 15 to enter a third compressor 13 to be boosted and heated, the third compressor 13 to be discharged from the third gas turbine 14 to be heated compressor 13 to be discharged from the third gas turbine 13 to be discharged as heat-discharged from the third gas turbine 10 to be discharged from the third gas turbine 358 to be discharged to be heated and the third gas turbine to be discharged to be heated and to be discharged to.

The -th class thermally driven compression-absorption heat pump shown in fig. 8 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a fourth compressor and a high-temperature heat regenerator; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with a condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with an evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9 through a high-temperature regenerator 18, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a second gas turbine 12 through, the third compressor 13 is also provided with a gas channel which is communicated with a fourth compressor 16 through the evaporator 4, the fourth compressor 16 is also provided with a gas channel which is communicated with a second compressor 11 through a heat supplier 14, the second compressor 11 is also provided with a gas channel which is communicated with the outside through a generator 2, the absorber 1, the condenser 3 and the heat supplier 14 are also respectively communicated with the outside through heated medium pipelines, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10 and the second gas turbine 12 are connected with the compressor 8, the second compressor 11, the third compressor 13 and the fourth compressor 16 and transmit power.

(2) In the process, dilute solution of an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, heats the solution entering the generator to release refrigerant steam and is provided for a condenser 3, concentrated solution of the generator 2 enters the absorber 1 through the solution heat exchanger 7, absorbs the refrigerant steam and releases heat to a heated medium, the refrigerant steam of the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid of the condenser 3 is throttled by a throttle valve 5 and enters an evaporator 4, absorbs heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, flows through a high-temperature regenerator 18 to absorb heat and then enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with compressed air and is combusted into high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and does work, the fuel gas discharged from the gas turbine 10 flows through the high-temperature regenerator 18 to release heat and then enters a second gas turbine 12 to be decompressed, the fuel gas discharged from the second gas turbine 12 flows through a low-temperature heat exchanger 15 to be heated and then enters a third compressor 13 to be boosted and heated, the third compressor 13 to discharge heat compressor 13 to discharge the heat compressor 3516 to discharge the fourth gas turbine 16 to discharge heat compressor 16 to form a fourth heat compressor 16 to discharge compressor 11 and discharge power compressor 3516 to discharge heat compressor 11 to discharge the third compressor 11 to discharge the heat compressor 11 and discharge compressor 11 to discharge the third compressor 11 to discharge the heat.

The -th class thermally driven compression-absorption heat pump shown in fig. 9 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a heat supplier, a low-temperature heat exchanger, a third gas turbine, a high-temperature heat regenerator and a fourth gas turbine; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with a condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with an evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9 through a high-temperature regenerator 18, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a second gas turbine 12 through the, the third gas turbine 17 is also provided with a gas channel which is communicated with a fourth gas turbine 19 through the evaporator 4, the fourth gas turbine 19 is also provided with a gas channel which is communicated with a second compressor 11 through a low-temperature heat exchanger 15, the second compressor 11 is also provided with a gas channel which is communicated with the outside through a generator 2, the absorber 1, the condenser 3 and the heat supplier 14 are also respectively provided with a heated medium pipeline which is communicated with the outside, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10, the second gas turbine 12, the third gas turbine 17 and the fourth gas turbine 19 are connected with the compressor 8 and the second compressor 11 and transmit power.

(2) In the process, dilute solution of an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, gas flows through the generator 2, heats the solution entering the generator to release refrigerant steam and provide the refrigerant steam to a condenser 3, concentrated solution of the generator 2 enters the absorber 1 through the solution heat exchanger 7, absorbs the refrigerant steam and releases heat to a heated medium, the refrigerant steam of the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid of the condenser 3 is throttled by a throttle valve 5 to enter an evaporator 4, absorbs heat to form the refrigerant steam and provides the refrigerant steam to the absorber 1, air enters a compressor 8 to be boosted and heated, flows through a high-temperature regenerator 18 to absorb heat and then enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with compressed air and is combusted into high-temperature gas, the high-temperature gas turbine 10 to be decompressed and powered, the gas discharged from the gas turbine 10 flows through the high-temperature regenerator 18 to release heat and then enters a second gas turbine 12 to be decompressed, the gas discharged from the second gas turbine 12 flows through a heat exchanger 14 to be decompressed and then enters a third gas turbine 17 to be decompressed and to be powered, the third gas turbine 17 to be discharged from a fourth gas turbine 19 to be powered, the absorption turbine 17 to be discharged from a fourth gas turbine 11 to be discharged from a fourth gas turbine 3511 to be heated, and discharged from a fourth gas turbine 11 to be heated compressor 11 to be discharged to be heated, and discharged to be heated.

The -th class thermally driven compression-absorption heat pump shown in fig. 10 is realized by:

(1) structurally, the system mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is also provided with a refrigerant steam channel which is communicated with a condenser 3, the condenser 3 is also provided with a refrigerant liquid pipeline which is communicated with an evaporator 4 through a throttle valve 5, the evaporator 4 is also provided with a refrigerant steam channel which is communicated with the absorber 1, an air channel is arranged outside and communicated with a compressor 8, the compressor 8 is also provided with a compressed air channel which is communicated with a combustion chamber 9 through a high-temperature regenerator 18, the combustion chamber 9 is also provided with a fuel channel which is communicated with the outside, the combustion chamber 9 is also provided with a fuel gas channel which is communicated with a gas turbine 10, the gas turbine 10 is also provided with a fuel gas channel which is communicated with a second gas turbine 12 through the high-temperature regenerator 18, the second gas turbine 12 is also provided with a third compressor 13, the third gas turbine 17 is also provided with a gas channel which is communicated with the second compressor 11 through a low-temperature heat exchanger 15, the second compressor 11 is also provided with a gas channel which is communicated with the outside through a generator 2, the absorber 1, the condenser 3 and the heat supplier 14 are also respectively provided with a heated medium pipeline which is communicated with the outside, the low-temperature heat exchanger 15 is also provided with a low-temperature heat medium channel which is communicated with the outside, and the gas turbine 10, the second gas turbine 12 and the third gas turbine 17 are connected with the compressor 8, the second compressor 11 and the third compressor 13 and transmit power.

(2) In the process, dilute solution in an absorber 1 enters a generator 2 through a solution pump 6 and a solution heat exchanger 7, fuel gas flows through the generator 2, heats the solution entering the generator to release refrigerant steam and is provided for a condenser 3, concentrated solution in the generator 2 enters the absorber 1 through the solution heat exchanger 7, absorbs the refrigerant steam and releases heat to a heated medium, the refrigerant steam in the condenser 3 releases heat to the heated medium to form refrigerant liquid, the refrigerant liquid in the condenser 3 is throttled by a throttle valve 5 and enters an evaporator 4 to absorb heat to form the refrigerant steam and is provided for the absorber 1, air enters a compressor 8 to be boosted and heated, flows through a high-temperature regenerator 18 to absorb heat and then enters a combustion chamber 9, external fuel enters the combustion chamber 9 to be mixed with compressed air and is combusted into high-temperature fuel gas, the high-temperature fuel gas enters a gas turbine 10 to be decompressed and does work, the fuel gas discharged from the gas turbine 10 flows through the high-temperature regenerator 18 to release heat and then enters a second gas turbine 12 to be decompressed, the fuel gas discharged from the second gas turbine 12 flows through the evaporator 4 to be boosted and heated and then enters a third compressor 13 to be boosted and heated, the third compressor 13 to be discharged from the third gas turbine 13 to be heated, flows through a heat exchanger 14 to be discharged from the third gas turbine 13 to be discharged to form a third gas turbine 13 to be discharged as heat exchanger 3511 to be discharged from the third gas turbine 13 to be discharged to be heated and the third gas turbine 11 to be discharged to be used as heat exchanger 3511 to be discharged.

The -th class thermally driven compression-absorption heat pump shown in fig. 11 is realized by:

in the -class heat-driven compression-absorption heat pump shown in fig. 1, a fuel channel which is externally communicated with a combustion chamber 9 is eliminated, a newly added compressor is added, a gaseous fuel channel which is externally communicated with the newly added compressor 20 is arranged, the newly added compressor 20 is also communicated with the combustion chamber 9, and a gas turbine 10 is connected with the newly added compressor 20 and transmits power to form a -class heat-driven compression-absorption heat pump.

The -th class thermally driven compression-absorption heat pump shown in fig. 12 is realized by:

in the type heat-driven compression-absorption heat pump shown in fig. 1, a second heat supply device is added, a fuel gas channel of the second compressor 11 is communicated with the outside through a generator 2, the second heat supply device 21 is adjusted to be communicated with the outside through a fuel gas channel of the second compressor 11, the fuel gas channel of the evaporator 4 is communicated with the outside after the generator 2, the second heat supply device 21 and the evaporator 4 are sequentially communicated, the fuel gas discharged by the second compressor 11 sequentially flows through the generator 2, the second heat supply device 21 and the evaporator 4 and gradually releases heat, and then the fuel gas is discharged to the outside, so that the type heat-driven compression-absorption heat pump is formed.

The -th class thermally driven compression-absorption heat pump shown in fig. 13 is realized by:

(1) structurally, in an type thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added, a dilute solution pipeline is additionally arranged on an absorber 1 and is communicated with the second generator 22 through a second solution pump 24 and a second solution heat exchanger 25, the second generator 22 and a concentrated solution pipeline are communicated with the absorber 1 through the second solution heat exchanger 25, a refrigerant steam channel of a generator 2 is communicated with a condenser 3 and is adjusted to be communicated with the second generator 22, then the refrigerant liquid pipeline of the second generator 22 is communicated with the condenser 3 through the second throttle valve 23, and the refrigerant steam channel of the second generator 22 is communicated with the condenser 3.

(2) In the process, refrigerant steam generated by the generator 2 is provided for the second generator 22 to serve as a driving heat medium, part of dilute solution in the absorber 1 enters the second generator 22 through the second solution pump 24 and the second solution heat exchanger 25, the refrigerant steam flows through the second generator 22, heats the solution entering the second generator 22 to release the refrigerant steam and provide the refrigerant steam for the condenser 3, concentrated solution in the second generator 22 enters the absorber 1 through the second solution heat exchanger 25, the refrigerant steam flowing through the second generator 22 releases heat to form refrigerant liquid, and then the refrigerant liquid enters the condenser 3 through the throttling of the second throttling valve 23 to form the -type heat-driven compression-absorption heat pump.

The -th class thermally driven compression-absorption heat pump shown in fig. 14 is realized by:

(1) structurally, in the type heat-driven compression-absorption heat pump shown in fig. 1, a second generator, a second throttle valve and a second solution heat exchanger are added, a dilute solution pipeline of an absorber 1 is communicated with a generator 2 through a solution pump 6 and a solution heat exchanger 7 and is adjusted to be communicated with the generator 2 through the solution pump 6, the solution heat exchanger 7 and a second solution heat exchanger 25, a concentrated solution pipeline of the generator 2 is communicated with the absorber 1 through the solution heat exchanger 7 and is adjusted to be communicated with the generator 1 through a concentrated solution pipeline of the generator 2 through the second solution heat exchanger 25 and is communicated with a second generator 22, a concentrated solution pipeline of the second generator 22 is communicated with the absorber 1 through the solution heat exchanger 7, a refrigerant vapor channel of the generator 2 is communicated with a condenser 3 through the refrigerant vapor channel of the generator 2 and is adjusted to be communicated with the second generator 22, a refrigerant liquid pipeline of the second generator 22 is communicated with the condenser 3 through the second throttle valve 23, and the second generator 22 is also communicated with the condenser 3 through the refrigerant vapor channel.

(2) In the process, refrigerant steam generated by the generator 2 is supplied to the second generator 22 to be used as a driving heat medium, dilute solution in the absorber 1 enters the generator 2 through the solution pump 6, the solution heat exchanger 7 and the second solution heat exchanger 25, concentrated solution in the generator 2 enters the second generator 22 through the second solution heat exchanger 25, the refrigerant steam flows through the second generator 22, heats the solution entering the second generator 22 to release the refrigerant steam and is supplied to the condenser 3, concentrated solution in the second generator 22 enters the absorber 1 through the solution heat exchanger 7, the refrigerant steam flowing through the second generator 22 releases heat to form refrigerant liquid, and then the refrigerant liquid flows into the condenser 3 through the second throttling valve 23 in a throttling mode to form the type heat driving compression-absorption heat pump.

The -th class thermally driven compression-absorption heat pump shown in fig. 15 is realized by:

(1) structurally, in the type thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added, a dilute solution pipeline of the absorber 1 is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7 and is adjusted to be communicated with the second generator 22 through the solution pump 6 and the solution heat exchanger 7, a concentrated solution pipeline of the second generator 22 is communicated with the generator 2 through a second solution pump 24 and a second solution heat exchanger 25, a concentrated solution pipeline of the generator 2 is communicated with the absorber 1 through the solution heat exchanger 7 and is adjusted to be communicated with the absorber 1 through a concentrated solution pipeline of the generator 2 through the second solution heat exchanger 25 and the solution heat exchanger 7, a refrigerant vapor channel of the generator 2 is communicated with the condenser 3 and is adjusted to be communicated with the second generator 22 through a refrigerant vapor channel of the generator 2 and is communicated with the condenser 3 through a second throttle valve 23, and a refrigerant vapor channel of the second generator 22 is communicated with the condenser 3.

(2) In the process, refrigerant steam generated by the generator 2 is provided to the second generator 22 as a driving heat medium, dilute solution in the absorber 1 enters the second generator 22 through the solution pump 6 and the solution heat exchanger 7, the refrigerant steam flows through the second generator 22, heats the solution entering the second generator 22 to release the refrigerant steam and provide the refrigerant steam to the condenser 3, concentrated solution in the second generator 22 enters the generator 2 through the second solution pump 24 and the second solution heat exchanger 25, concentrated solution in the generator 2 enters the absorber 1 through the second solution heat exchanger 25 and the solution heat exchanger 7, the refrigerant steam flowing through the second generator 22 releases heat to form refrigerant liquid, and then the refrigerant liquid is throttled by the second throttle valve 23 to enter the condenser 3 to form the type heat driving compression-absorption heat pump.

The -th class thermally driven compression-absorption heat pump shown in fig. 16 is realized by:

in the heat-driven compression-absorption heat pump shown in fig. 14, a second heat supply device is added, a fuel gas channel of the second compressor 11 is communicated with the outside through a generator 2, the second compressor 11 is adjusted to be communicated with the outside through a fuel gas channel, the generator 2, a second generator 22, a second heat supply device 21 and an evaporator 4 are sequentially communicated, then the evaporator 4 is provided with a fuel gas channel, the fuel gas channel is communicated with the outside, the second heat supply device 21 is also communicated with the outside through a heated medium channel, the fuel gas discharged from the second compressor 11 sequentially flows through the generator 2, the second generator 22, the second heat supply device 21 and the evaporator 4 and gradually releases heat, and then the fuel gas is discharged to the outside, so that the heat-driven compression-absorption heat pump is formed.

The -th class thermally driven compression-absorption heat pump shown in fig. 17 is realized by:

(1) structurally, in the -class thermally-driven compression-absorption heat pump shown in fig. 1, a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added, the evaporator 4 is adjusted to be communicated with the absorber 1 through a refrigerant steam channel, the evaporator 4 is adjusted to be communicated with the second absorber 26 through the refrigerant steam channel, the second absorber 26 is also provided with a dilute solution pipeline which is communicated with the second generator 22 through a second solution pump 24 and a second solution heat exchanger 25, the second generator 22 is also provided with a concentrated solution pipeline which is communicated with the second absorber 26 through the second solution heat exchanger 25, the second generator 22 is also provided with a refrigerant steam channel which is communicated with the absorber 1, the second compressor 11 is adjusted to be communicated with the outside through the generator 2 through a gas channel, the second compressor 11 is sequentially communicated with the generator 2 and the second generator 22 through a gas channel, then the second generator 22 is further provided with the outside through a gas channel, and the second absorber 26 is also provided with a heated medium channel which is communicated with the outside.

(2) In the flow process, refrigerant steam generated by the evaporator 4 enters a second absorber 26, dilute solution of the second absorber 26 enters a second generator 22 through a second solution pump 24 and a second solution heat exchanger 25, fuel gas flows through the second generator 22, heats the solution entering the second generator 22 to release the refrigerant steam and provide the refrigerant steam for the absorber 1, and concentrated solution of the second generator 22 enters the second absorber 26 through the second solution heat exchanger 25, absorbs the refrigerant steam and releases heat to a heated medium to form a -type thermally-driven compression-absorption heat pump.

The -th class thermally driven compression-absorption heat pump shown in fig. 18 is realized by:

(1) structurally, in an type heat-driven compression-absorption heat pump shown in fig. 1, a second generator, a second absorber, a second solution pump, a solution throttle valve, a second solution throttle valve and a steam-dividing chamber are added, wherein a dilute solution pipeline of the absorber 1 is communicated with the generator 2 through a solution pump 6 and a solution heat exchanger 7, so that the absorber 1 is adjusted to be communicated with a dilute solution pipeline through the solution pump 6 and the solution heat exchanger 7 and communicated with a second absorber 26, the second absorber 26 is also provided with a dilute solution pipeline communicated with the second generator 22 through a solution throttle valve 27, the second generator 22 is further provided with a concentrated solution pipeline communicated with the generator 2 through a second solution pump 24, the generator 2 is adjusted to be communicated with the absorber 1 through the solution heat exchanger 7, so that the generator 2 is provided with a concentrated solution pipeline communicated with the steam-dividing chamber 29 through a second solution throttle valve 28 and the second absorber 26, the steam-dividing chamber 29 is further provided with the concentrated solution pipeline communicated with the absorber 1 through the solution heat exchanger 7, the generator 2 is adjusted to be communicated with the condenser 3, so that the generator 2 is provided with a steam channel communicated with the second generator 26 and the second generator 22, and the steam-dividing chamber 29 are sequentially communicated with a gas-generating compressor 11, and a gas-generating compressor 22 are sequentially communicated with a gas-generating compressor 11.

(2) In the process, a dilute solution in the absorber 1 enters the second absorber 26 through the solution pump 6 and the solution heat exchanger 7, absorbs refrigerant steam and releases heat, the dilute solution in the second absorber 26 is throttled and depressurized through the solution throttle valve 27 and enters the second generator 22, fuel gas flows through the second generator 22, heats the solution entering the second generator 22, releases the refrigerant steam and is provided for the condenser 3, a concentrated solution in the second generator 22 enters the generator 2 through the second solution pump 24, the fuel gas flows through the generator 2, heats the solution entering the second generator, releases the refrigerant steam and is provided for the second absorber 26, the concentrated solution in the generator 2 is throttled and depressurized through the second solution throttle valve 28 and then flows through the second absorber 26 to absorb heat and partially vaporize, the solution after partial vaporization of the heat absorption enters the vapor distribution chamber 29, the vapor distribution chamber 29 releases the refrigerant steam and is provided for the condenser 3, and the concentrated solution in the vapor distribution chamber 29 enters the absorber 1 through the solution heat exchanger 7, so as to form the type heat-driven compression-heat.

The effect that the technology of the invention can realize-the type heat driving compression-absorption heat pump provided by the invention has the following effects and advantages:

(1) provides a new idea and a new technology for utilizing temperature difference under the condition of directly utilizing fuel as driving energy.

(2) The heat energy (temperature difference) drives to realize heat supply/refrigeration, or can selectively provide power to the outside at the same time.

(3) The compression heat pump flow bears partial heat supply load and low-temperature heat load extraction, and is favorable for realizing effective utilization of high-temperature section temperature difference and utilization level of full-temperature section temperature difference.

(4) The process is reasonable, the performance index is variable, thermodynamic parameter changes are corresponding, and the full and efficient utilization of heat energy (temperature difference) can be realized.

(5) When necessary, heat supply/refrigeration is realized by means of external power, the mode is flexible, and the adaptability is good.

(6) The gas turbine device is utilized to deal with the utilization of the temperature difference of the high-temperature section, and the high-efficiency utilization of the heat energy of the high-temperature section is effectively realized.

(7) The effective utilization of low-temperature heat energy is realized, the conflict between the parameters of the low-temperature heat medium and the performance of the refrigerant liquid is avoided, and the defects of the absorption heat pump technology are overcome.

(8) The gas is directly used as a working medium of a compression heat pump process, so that heat transfer links are reduced, the heat energy utilization efficiency is improved, and the equipment manufacturing cost is reduced.

(9) Compared with a heat-driven compression heat pump, the flow of the absorption heat pump is adopted to complete refrigerant steam pressure rise, moving parts are reduced, equipment safety is improved, and adverse effects on the environment are reduced.

(10) A plurality of specific technical schemes are provided, so that the method can cope with a plurality of different actual conditions and has a wider application range.

(11) The heat pump technology is expanded, the types of the compression-absorption heat pump are enriched, and the high-efficiency utilization of heat energy is favorably realized.

Claims

1. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger, wherein the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel which is communicated with the condenser (3), the condenser (3) is also provided with a refrigerant liquid pipeline which is communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel which is communicated with the gas turbine (1), an external air channel which is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel which is communicated with the combustion chamber (9), the combustion chamber (9) is also provided with a fuel channel which is communicated with the external, the combustion chamber (9) is also provided with a gas turbine (10), the gas turbine (10) is also provided with the second compressor (10), the heat exchanger (13) which is communicated with the gas turbine, the second compressor (13) and the gas turbine (13), the heat exchanger (13) is also provided with a heat exchanger (13), the gas turbine (10), the gas turbine (13), the heat exchanger (13) which is communicated with the second compressor, the heat exchanger (10) and the gas turbine (10), the heat exchanger (13) and the heat supplier, the heat exchanger (13) are respectively communicated with the heat exchanger (13), the heat exchanger (13) and the heat exchanger (13) which are also provided.

2. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger, wherein the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel which is communicated with the condenser (3), the condenser (3) is also provided with a refrigerant liquid pipeline which is communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel which is communicated with the gas turbine (1), an external air channel which is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel which is communicated with the combustion chamber (9), the combustion chamber (9) is also provided with a fuel channel which is communicated with the external, the combustion chamber (9) is also provided with a gas turbine (10), the gas turbine (10) is also provided with a second gas turbine, the heat exchanger (10) which is communicated with the second compressor (13), the gas turbine, the second compressor (13) is also provided with a heat exchanger (13) which is communicated with the gas turbine, the gas turbine (10), the gas turbine (13) and the heat exchanger (13), the heat exchanger (10) and the heat exchanger (13), the heat supplier, the gas turbine is also provided with the second gas turbine (13), the heat exchanger (13) and the heat exchanger (13), the heat exchanger (10), the compressor (13) are also provided with.

3. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a third compressor, a heat supply device, a low-temperature heat exchanger and a fourth compressor, wherein the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through a solution pump (6) and a solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel which is communicated with the condenser (3), the condenser (3) is also provided with a refrigerant liquid pipeline which is communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel which is communicated with the compressor (1), an external air channel which is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel which is communicated with the combustion chamber (9), the combustion chamber (9) is also provided with a fuel channel which is communicated with the external, the combustion chamber (9) is also provided with a gas turbine (10), the heat exchanger (10) is also provided with the heat supply device which is communicated with the second compressor (16), the fourth compressor (13), the heat exchanger, the heat compressor (16) and the fourth compressor (16) are also provided with the gas turbine (13) through a heat exchanger (16), the gas turbine (10), the heat compressor (13), the heat compressor (16) and the heat exchanger (16), the heat compressor (13) and the heat compressor (13), the heat compressor (16) and the heat compressor (16) are respectively communicated with the heat compressor (16), the heat compressor (16) through a heat compressor (13) and the heat compressor (13), the heat compressor (16) through a heat.

4. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a heat supply device, a low-temperature heat exchanger and a third gas turbine, wherein the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel which is communicated with the condenser (3), the condenser (3) is also provided with a refrigerant liquid pipeline which is communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel which is communicated with the gas turbine (1), an external air channel which is communicated with the absorber (8), the compressor (8) is also provided with a compressed air channel which is communicated with the combustion chamber (9), the combustion chamber (9) is also provided with a fuel channel which is communicated with the external, the combustion chamber (9) is also provided with a gas turbine (10), the gas turbine is also provided with a gas turbine (10), the second gas turbine, a heat exchanger (10) which is also provided with a second gas turbine, a second gas turbine (17) which is communicated with a second gas turbine, a heat transfer medium which is communicated with the gas turbine (17), a second gas turbine (17), a heat exchanger (10) which is communicated with the gas turbine (17), a second gas turbine (10) which is communicated with the gas turbine, a heat exchanger (17) which is communicated with the gas turbine (17) and a second gas turbine (17), and a heat exchanger (17), and a heat transfer pipeline which is communicated with the gas turbine (17), and a heat exchanger (17), and a second gas turbine (17), the gas.

5. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier and a low-temperature heat exchanger, wherein the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel which is communicated with the condenser (3), the condenser (3) is also provided with a refrigerant liquid pipeline which is communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel which is communicated with the gas turbine (1), an external air channel which is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel which is communicated with the combustion chamber (9), the combustion chamber (9) is also provided with a fuel channel which is communicated with the external, the combustion chamber (9) is also provided with a gas turbine (10), the gas turbine (10) is also provided with the second compressor (13), the gas turbine, the second compressor is also provided with a heat exchanger (10) which is communicated with a heat exchanger (13), the gas turbine (13) which is communicated with the second gas turbine (10), the gas turbine (13), the gas turbine, the second compressor (13) and the heat exchanger (10) and the heat exchanger (13), the heat exchanger (13) are also provided with the gas turbine (13), the heat exchanger (13) and the heat exchanger (13), the heat exchanger (13) and the heat exchanger (10) are also provided with the heat exchanger (13) which are.

6. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator, wherein the absorber (1) is provided with a dilute solution pipeline communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel communicated with the condenser (3), the condenser (3) is also provided with a liquid turbine pipeline communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel communicated with the absorber (1), an external air channel is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel communicated with the combustion chamber (9) through the high-temperature heat turbine (18), the combustion chamber (9) is also provided with a fuel channel communicated with the absorber (10), the gas turbine (10) is also communicated with the third gas turbine (10), the gas turbine (10) and the gas turbine (10), the gas turbine is also provided with the heat exchanger (13), the gas turbine (10) and the gas turbine (13), the gas turbine is also provided with the heat exchanger (10), the compressor (13), the gas turbine (17), the compressor (17), the gas turbine is also provided with the heat exchanger (13), the gas turbine (17) and the heat exchanger, the gas turbine (10), the gas turbine (17), the gas turbine is also provided with the gas turbine (17), the gas turbine and the heat exchanger (17), the gas turbine (17), the compressor (17), the gas turbine and the gas turbine (17) and the gas turbine are also provided with the heat exchanger, the gas turbine, the gas compressor (17) and the gas turbine, the gas turbine are also provided with the gas turbine, the.

7. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator, wherein the absorber (1) is provided with a dilute solution pipeline communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel communicated with the condenser (3), the condenser (3) is also provided with a liquid turbine pipeline communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel communicated with the absorber (1), an external air channel is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel communicated with the combustion chamber (9) through the high-temperature heat turbine (18), the combustion chamber (9) is also provided with a fuel channel communicated with the absorber (10), the gas turbine (10) is also communicated with the third gas turbine (10), the gas turbine (10) and the gas turbine (13), the gas turbine is also provided with the heat exchanger (10), the gas turbine (13), the gas turbine is also provided with the heat exchanger (10) and the heat exchanger (13), the compressor (13), the gas turbine (10), the compressor (13), the compressor (17), the gas turbine is also provided with the gas turbine (13), the heat exchanger, the compressor (17) and the gas turbine (13), the gas turbine is also provided with the gas turbine (17), the gas turbine (13), the gas turbine (10) and the gas turbine, the gas turbine (17) and the gas turbine are also provided with the heat exchanger (17) and the gas turbine, the gas compressor (17) and the gas turbine, the gas turbine (17) and the gas turbine.

8. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a fourth compressor and a high-temperature heat regenerator, wherein the absorber (1) is provided with a dilute solution pipeline communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel communicated with the condenser (3), the condenser (3) is also provided with a liquid pipeline communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel communicated with the absorber (1), an external air channel is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel communicated with the combustion chamber (9) through the high-temperature heat turbine (18), the combustion chamber (9) is also provided with a fuel channel communicated with the absorber (10), the second gas turbine is also provided with the heat exchanger (10), the heat exchanger (10) is also provided with a heat exchanger (16), the gas turbine (10), the compressor (16) is also provided with the heat exchanger (13), the compressor (10) and the compressor (13), the compressor (16) and the compressor (13), the compressor is also provided with the compressor (16), the compressor (13) and the compressor, the compressor (16) and the heat exchanger is also provided with the heat exchanger (10) and the heat exchanger, the heat exchanger (10) and the compressor, the compressor (16) and the compressor are also provided with the compressor, the compressor (16) and the compressor, the compressor (10) are also provided with the compressor, the heat exchanger (16) and the heat exchanger (10) respectively communicated with the compressor, the.

9. The type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a heat supply device, a low-temperature heat exchanger, a third gas turbine, a high-temperature heat regenerator and a fourth gas turbine, wherein the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel which is communicated with the condenser (3), the condenser (3) is also provided with a liquid pipeline of the turbine which is communicated with the evaporator (4) through the throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel which is communicated with the absorber (1), an external air channel which is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel which is also communicated with the combustion chamber (9) through the high-temperature heat turbine (18), the combustion chamber (9) is also provided with a heat turbine channel which is communicated with the second gas turbine, a heat exchanger (10) which is also provided with a heat exchanger (10), a heat exchanger (17), a fourth gas turbine channel which is communicated with a gas turbine (10) which is communicated with a heat exchanger (10), a gas turbine (17), and a gas turbine (17), the gas turbine (19) which is also communicated with a heat exchanger (10) which is also communicated with a fourth gas turbine, a gas turbine (17) which is communicated with a gas turbine, a gas turbine (10) which is also communicated with a heat exchanger (10) which is communicated with a gas turbine, and a gas turbine, a gas turbine (17) which is communicated with a gas turbine, a heat exchanger (10) which is also communicated with a gas turbine, a gas turbine (10) which is communicated with a gas.

10. A type heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a compressor, a combustion chamber, a gas turbine, a second compressor, a second gas turbine, a third compressor, a heat supplier, a low-temperature heat exchanger, a third gas turbine and a high-temperature heat regenerator, wherein the absorber (1) is provided with a dilute solution pipeline communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7), the generator (2) is also provided with a concentrated solution pipeline communicated with the absorber (1) through the solution heat exchanger (7), the generator (2) is also provided with a refrigerant steam channel communicated with the condenser (3), the condenser (3) is also provided with a liquid turbine pipeline communicated with the evaporator (4) through a throttle valve (5), the evaporator (4) is also provided with a refrigerant steam channel communicated with the absorber (1), an external air channel is communicated with the compressor (8), the compressor (8) is also provided with a compressed air channel communicated with the combustion chamber (9) through the high-temperature heat turbine (18), the combustion chamber (9) is also provided with a fuel channel communicated with the absorber (10), the gas turbine is also communicated with the third gas turbine (10), the gas turbine (10) and the heat exchanger (10), the gas turbine is also provided with the gas turbine (10), the gas turbine (13), the third gas turbine is also provided with the gas turbine (10) and the heat exchanger (10), the gas turbine (13), the gas turbine is also provided with the gas turbine (13), the gas turbine (17), the gas turbine is also provided with the gas turbine and the gas turbine (13), the gas turbine (17), the gas turbine (13), the gas turbine (10) and the gas turbine (17), the gas turbine (17) and the gas turbine are also provided with the gas compressor (17) and the gas turbine, the gas turbine (17) and the.

11. A -class heat-driven compression-absorption heat pump, which is the - -class heat-driven compression-absorption heat pump as claimed in claims 1-10, wherein a fuel channel communicated with a combustion chamber (9) is eliminated from the outside, a newly added compressor is added, a gaseous fuel channel is arranged on the outside and communicated with the newly added compressor (20), the newly added compressor (20) is also communicated with the combustion chamber (9) through a compressed gaseous fuel channel, and a gas turbine (10) is connected with the newly added compressor (20) and transmits power to form the -class heat-driven compression-absorption heat pump.

12. An class heat-driven compression-absorption heat pump, which is the class heat-driven compression-absorption heat pump of claims 1-11, wherein a second heat supply device is added, the second compressor (11) is provided with a fuel gas channel which is communicated with the outside through a generator (2) and adjusted to be that the second compressor (11) is provided with a fuel gas channel which is communicated with the generator (2) and the second heat supply device (21) in sequence, then the second heat supply device (21) is provided with a fuel gas channel which is communicated with the outside, and the second heat supply device (21) is also provided with a heated medium channel which is communicated with the outside to form the class heat-driven compression-absorption heat pump.

13. A th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump of claims 1-11, wherein a second heat supply device is added, the second compressor (11) is provided with a fuel gas channel which is communicated with the outside through a generator (2) and is adjusted to be that the second compressor (11) is provided with a fuel gas channel which is communicated with the generator (2), the second heat supply device (21) and an evaporator (4), then the evaporator (4) is provided with a fuel gas channel which is communicated with the outside, the second heat supply device (21) is also provided with a heated medium channel which is communicated with the outside, and the th class heat-driven compression-absorption heat pump is formed.

14. An th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump as claimed in claims 1-11, wherein a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added, the absorber (1) is additionally provided with a dilute solution pipeline which is communicated with the second generator (22) through the second solution pump (24) and the second solution heat exchanger (25), the second generator (22) and a concentrated solution pipeline are communicated with the absorber (1) through the second solution heat exchanger (25), the generator (2) is provided with a refrigerant steam channel which is communicated with the condenser (3) and is adjusted to be communicated with the condenser (3) after the generator (2) is provided with a refrigerant steam channel which is communicated with the second generator (22), the second generator (22) is further provided with a refrigerant liquid pipeline which is communicated with the condenser (3) through the second throttle valve (23), and the second generator (22) is further provided with a refrigerant steam channel which is communicated with the condenser (3), thereby forming the class heat-driven compression-absorption heat pump.

15. A class heat-driven compression-absorption heat pump, wherein a second generator, a second throttle valve and a second solution heat exchanger are added to any class heat-driven compression-absorption heat pump as claimed in claims 1 to 11, the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7) and is adjusted to be a dilute solution pipeline which is communicated with the absorber (1) through the solution pump (6), the solution heat exchanger (7) and the second solution heat exchanger (25) to be a generator (2), the generator (2) is provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7) and is adjusted to be a generator (2) which is provided with a concentrated solution pipeline which is communicated with the second generator (22) through the second solution heat exchanger (25), the second generator (22) is further provided with the absorber (1) through the solution heat exchanger (7), the generator (2) is adjusted to be a condenser (2) which is provided with a steam pipeline which is communicated with the second generator (22), and a second heat-generator (22) which is further communicated with a second heat-generator (23) through a steam-driven heat pump and a second condenser (3) which is also communicated with a second heat-generator (3) through a second steam-driven condenser (23).

16. A class thermally driven compression-absorption heat pump, wherein a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added to any class thermally driven compression-absorption heat pump according to claims 1 to 11, the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through the solution pump (6) and the solution heat exchanger (7) and is adjusted to be communicated with the absorber (1) through the solution pump (6) and the solution heat exchanger (7), the second generator (22) is further provided with a concentrated solution pipeline which is communicated with the generator (2) through the second solution pump (24) and the second solution heat exchanger (25), the generator (2) is provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (7) and is adjusted to be communicated with the generator (2) which is provided with a concentrated solution pipeline which is communicated with the generator (1) through the second solution heat exchanger (25) and the solution heat exchanger (7), the generator (2) is adjusted to be communicated with the generator (2) which is provided with the concentrated solution pipeline which is communicated with the second solution heat exchanger (25) and the second solution heat exchanger (7), the generator (2) is adjusted to be communicated with the second generator (22), and is also communicated with the second heat pump (3) through the second generator and the second condenser (23), and the second heat exchanger (3), and the second generator (3) are communicated with the second heat pump ).

17. A th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump as claimed in claims 14-16, wherein a second heat supply device is added, the second compressor (11) is adjusted to be communicated with the outside through a gas channel of a generator (2), after the second compressor (11) is sequentially communicated with the generator (2) and the second heat supply device (21) through the gas channel, the second heat supply device (21) is further communicated with the outside through the gas channel, and a heated medium channel is also communicated with the outside, so as to form the th class heat-driven compression-absorption heat pump.

18. A th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump of claims 14-16, wherein a second heat supply device is added, the second compressor (11) is provided with a fuel gas channel which is communicated with the outside through a generator (2) and is adjusted to be that the second compressor (11) is provided with a fuel gas channel which is communicated with the generator (2), the second heat supply device (21) and an evaporator (4) in sequence, then the evaporator (4) is provided with a fuel gas channel which is communicated with the outside, the second heat supply device (21) is also provided with a heated medium channel which is communicated with the outside, and the th class heat-driven compression-absorption heat pump is formed.

19. An th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump as claimed in claims 14-16, wherein the second compressor (11) is adjusted to have a fuel gas channel communicated with the outside through the generator (2) so that the second compressor (11) has a fuel gas channel communicated with the generator (2) and the second generator (22) in turn, and then the second generator (22) has a fuel gas channel communicated with the outside, thereby forming the th class heat-driven compression-absorption heat pump.

20. An class heat-driven compression-absorption heat pump, which is the class heat-driven compression-absorption heat pump of claims 14-16, wherein a second heat supply device is added, the second compressor (11) is provided with a fuel gas channel which is communicated with the outside through a generator (2) and adjusted to be that the second compressor (11) is provided with a fuel gas channel which is communicated with the generator (2), the second generator (22) and the second heat supply device (21) in sequence, then the second heat supply device (21) is provided with a fuel gas channel which is communicated with the outside, and the second heat supply device (21) is also provided with a heated medium channel which is communicated with the outside to form the class heat-driven compression-absorption heat pump.

21. A -class heat-driven compression-absorption heat pump, which is the - -class heat-driven compression-absorption heat pump as claimed in claims 14-16, wherein a second heat supply device is added, the second compressor (11) is communicated with the outside through a gas channel via a generator (2) and is adjusted to be that the second compressor (11) is communicated with the outside through a gas channel which is sequentially communicated with the generator (2), the second generator (22), the second heat supply device (21) and the evaporator (4), then the evaporator (4) is further communicated with the outside through a gas channel, and the second heat supply device (21) is also communicated with the outside through a heated medium channel to form the -class heat-driven compression-absorption heat pump.

22. A class heat-driven compression-absorption heat pump, which is characterized in that a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added in any class heat-driven compression-absorption heat pump of claims 1 to 11, an evaporator (4) is provided with a refrigerant vapor passage to communicate with the absorber (1) and is adjusted to communicate with the evaporator (4) with the refrigerant vapor passage to communicate with the second absorber (26), the second absorber (26) is also provided with a dilute solution pipeline to communicate with the second generator (22) through the second solution pump (24) and the second solution heat exchanger (25), the second generator (22) is also provided with a concentrated solution pipeline to communicate with the second absorber (26) through the second solution heat exchanger (25), the second generator (22) is also provided with the refrigerant vapor passage to communicate with the absorber (1), the second compressor (11) is provided with a gas passage to communicate with the outside through the generator (2) and is adjusted to communicate with the second compressor (11) through the gas passage to sequentially communicate with the generator (2) and the second generator (22) and the second absorber (22), and is also communicated with the external heat-absorption heat pump, and is also provided with the second generator (35) and is also communicated with the external heat-absorption heat pump.

23. A class heat-driven compression-absorption heat pump, wherein a second generator, a second absorber, a second solution pump, a solution throttle valve, a second solution throttle valve and a vapor distribution chamber are added in any class heat-driven compression-absorption heat pump as claimed in claims 1 to 11, the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through a solution pump (6) and a solution heat exchanger (7) and adjusted to be that the absorber (1) is provided with a dilute solution pipeline which is communicated with the second absorber (26) through the solution pump (6) and the solution heat exchanger (7), the second absorber (26) is also provided with a dilute solution pipeline which is communicated with the second generator (22) through a solution throttle valve (27), the second generator (22) is further provided with a concentrated solution pipeline which is communicated with the generator (2) through a second solution pump (24), the generator (2) is provided with the absorber (1) through a solution heat exchanger (7) and adjusted to be that the generator (2) is provided with a concentrated solution pipeline which is communicated with the generator (2) through a second solution throttle valve (28) and the second generator (2), the vapor generator (29) is also communicated with the vapor generator (2) through a vapor generation compressor, the vapor generation compressor (29) and a vapor generation chamber, the vapor generator (29) is also communicated with a vapor generator (2), the vapor generator (2) and a vapor generator (2) is also communicated with a vapor generator (2), and a vapor generator (26), the vapor generator (2), the vapor generator (29), the vapor generator (2), the vapor generator is also communicated with a vapor compressor, the vapor generator (2), the vapor generator is also communicated with a.

24. A th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump as claimed in any one of claims 1 to 23, wherein a power machine is added, the power machine is connected with the second compressor (11) and transmits power to the second compressor (11), and thus, a th class heat-driven compression-absorption heat pump driven by additional external power is formed.

25. A th class heat-driven compression-absorption heat pump, which is the th class heat-driven compression-absorption heat pump as claimed in claims 1-23, wherein a working machine is added, and a gas turbine (10) is connected with the working machine and transmits power to the working machine to form a th class heat-driven compression-absorption heat pump for additionally providing power load to the outside.