Fourth-type thermally-driven compression-injection-absorption heat pump

Abstract

The invention provides a fourth-class compression-injection-absorption heat pump, and belongs to the field of heat pumps. The low-temperature generator is communicated with the high-temperature generator through the solution pump, the solution heat exchanger and the second solution heat exchanger, the high-temperature generator is communicated with the low-temperature generator through the second solution heat exchanger, the absorber and the solution heat exchanger, and the low-temperature generator is communicated with the low-temperature condenser, the low-pressure pump and the evaporator. A high-temperature generator is communicated with a compressor, a high-temperature heat exchanger, an expansion machine and a high-temperature condenser, the high-temperature condenser is communicated with an evaporator through a low-temperature generator and a throttling valve and communicated with a steam generator and a high-pressure steam opening of an ejector through a high-pressure pump, the evaporator is communicated with a low-pressure steam opening of the ejector, and the ejector is communicated with an absorber. The high-temperature generator, the high-temperature heat exchanger and the steam generator are communicated with the outside through high-temperature heat medium channels, the absorber and the high-temperature condenser are communicated with the outside through heated medium channels, the low-temperature condenser is communicated with the outside through a cooling medium channel, and the evaporator is communicated with the outside through a low-temperature heat medium pipeline.

Description

Technical fields:

[0001] This invention belongs to the field of refrigeration and heat pump technology. Background technology:

[0002] People need to utilize energy for cooling and efficient heating, with heat energy being a conventional technology. In practical applications, the operating parameters, performance index, and manufacturing cost of heat pumps need to be given priority and emphasis.

[0003] In refrigeration / heating technology, steam jet refrigeration devices have the advantages of simple structure, reliable operation, low investment, and long service life; however, their disadvantages are that the utilization efficiency of the driving steam needs to be improved, and the heating temperature is limited.

[0004] Absorption refrigeration / heat pump technology also has the advantages of low manufacturing cost and the ability to directly use thermal energy as a driving energy source; however, its working range and application fields are greatly limited by the properties of the solution and refrigerant medium.

[0005] Based on the principles of simple, proactive, and efficient utilization of thermal energy or combined thermal and mechanical energy for refrigeration / heating, this invention proposes a fourth type of heat-driven compression-ejection-absorption heat pump, which features a reasonable process, simple structure, low cost, wide operating range, and achieves technological integration and rationalized performance index. Summary of the Invention:

[0006] The main objective of this invention is to provide a fourth type of heat-driven compression-ejection-absorption heat pump, the specific contents of which are described below:

[0007] 1. The fourth type of heat-driven compression-ejection-absorption heat pump mainly consists of a low-temperature generator, a solution pump, a solution heat exchanger, a second solution heat exchanger, a high-temperature generator, an absorber, a low-temperature condenser, a low-pressure pump, an evaporator, a compressor, a high-temperature heat exchanger, an expander, a high-temperature condenser, a throttling valve, a high-pressure pump, a steam generator, and an ejector. The low-temperature generator has a concentrated solution pipeline connected to the high-temperature generator via the solution pump, the solution heat exchanger, and the second solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution heat exchanger. The absorber also has a dilute solution pipeline connected to the low-temperature generator via the solution heat exchanger. The low-temperature generator also has a refrigerant vapor channel connected to the low-temperature condenser. The low-temperature condenser also has a refrigerant liquid pipeline connected to the evaporator via the low-pressure pump. The high-temperature generator also has a refrigerant vapor channel connected to the compressor. The compressor also has a refrigerant vapor channel connected to the compressor. The refrigerant vapor channel is connected to the expander via a high-temperature heat exchanger. The expander also has a refrigerant vapor channel connected to the high-temperature condenser. The high-temperature condenser also has a refrigerant liquid pipeline connected to the evaporator via a low-temperature generator and a throttling valve. The high-temperature condenser also has a refrigerant liquid pipeline connected to the steam generator via a high-pressure pump. The steam generator also has a refrigerant vapor channel connected to the high-pressure steam inlet of the ejector. The evaporator also has a refrigerant vapor channel connected to the low-pressure steam inlet of the ejector. The ejector also has a medium-pressure refrigerant vapor channel connected to the absorber. The high-temperature generator, high-temperature heat exchanger, and steam generator also have high-temperature heat medium channels connected to the outside. The absorber and high-temperature condenser also have heated medium channels connected to the outside. The low-temperature condenser also has a cooling medium channel connected to the outside. The evaporator also has a low-temperature heat medium channel connected to the outside, forming a fourth type of heat-driven compression-ejection-absorption heat pump.

[0008] 2. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in item 1, with the addition of a regenerator. The refrigerant vapor passage of the compressor is changed from being connected to the expander via a high-temperature heat exchanger to being connected to the expander via a regenerator and a high-temperature heat exchanger. The refrigerant vapor passage of the expander is changed from being connected to the high-temperature condenser to being connected to the high-temperature condenser via a regenerator.

[0009] 3. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in item 1, with the addition of a regenerator. The compressor's refrigerant vapor passage is changed from being connected to the expander via a high-temperature heat exchanger to being connected to itself via the regenerator. Then, the compressor has a refrigerant vapor passage connected to the expander via a high-temperature heat exchanger. The expander's refrigerant vapor passage is changed from being connected to the high-temperature condenser to being connected to the high-temperature condenser via the regenerator, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0010] 4. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in item 1, with the addition of a regenerator. The refrigerant vapor passage of the compressor is changed from being connected to the expander via a high-temperature heat exchanger to being connected to the expander via the regenerator and the high-temperature heat exchanger. The refrigerant vapor passage of the expander is changed from being connected to the high-temperature condenser to being connected to the expander via the regenerator and itself, and then the expander has a refrigerant vapor passage connected to the high-temperature condenser, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0011] 5. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in item 1, with the addition of a regenerator and a second compressor. The compressor is modified so that it has a refrigerant vapor channel connected to the expander via a high-temperature heat exchanger, while the compressor has a refrigerant vapor channel connected to the expander via the regenerator and the high-temperature heat exchanger. An intermediate extraction steam channel is added to the expander, which is connected to the second compressor via the regenerator. The second compressor also has a refrigerant vapor channel connected to the expander via the high-temperature heat exchanger. The expander connects the compressor and the second compressor and transmits power, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0012] 6. A fourth type of heat-driven compression-ejection-absorption heat pump is formed by adding a second solution pump to any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in items 1-5. The connection between the low-temperature generator with a concentrated solution pipeline via the solution pump, solution heat exchanger, and second solution heat exchanger and the high-temperature generator is adjusted so that the low-temperature generator with a concentrated solution pipeline via the second solution pump and second solution heat exchanger and the absorber is connected to the absorber. The absorber then has a dilute solution pipeline via the solution pump and solution heat exchanger and is connected to the high-temperature generator. The connection between the high-temperature generator with a concentrated solution pipeline via the second solution heat exchanger and the absorber is adjusted so that the high-temperature generator with a concentrated solution pipeline via the solution heat exchanger and second solution heat exchanger and the low-temperature generator is connected to the low-temperature generator, thus forming a fourth type of heat-driven compression-ejection-absorption heat pump.

[0013] 7. The fourth type of heat-driven compression-ejection-absorption heat pump, in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in items 1-5, omits the low-temperature condenser and its cooling medium channel connected to the outside, omits the low-pressure pump, and omits the refrigerant liquid pipeline connecting the low-temperature condenser to the evaporator via the low-pressure pump; adds a second solution pump and a second absorber, and adjusts the connection between the low-temperature generator's concentrated solution pipeline and the high-temperature generator via the solution pump, solution heat exchanger, and second solution heat exchanger to a connection between the low-temperature generator's concentrated solution pipeline and the absorber via the second solution pump and solution heat exchanger. The absorber also... A dilute solution pipeline connects to the second absorber via a solution heat exchanger. The second absorber then has a dilute solution pipeline connecting to the solution pump and the high-temperature generator via the second solution heat exchanger. The high-temperature generator is then connected to the absorber via a concentrated solution pipeline via the second solution heat exchanger. Alternatively, the high-temperature generator can be connected to the low-temperature generator via a concentrated solution pipeline via the second solution heat exchanger. The low-temperature generator can be connected to the low-temperature condenser via a refrigerant vapor channel. Alternatively, the low-temperature generator can be connected to the second absorber via a refrigerant vapor channel. The second absorber also has a cooling medium channel connected to the outside, forming a fourth type of heat-driven compression-ejection-absorption heat pump.

[0014] 8. The fourth type of heat-driven compression-ejection-absorption heat pump is formed by eliminating the high-pressure pump and steam generator in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in items 1-7. The high-temperature condenser refrigerant liquid pipeline is connected to the steam generator via the high-pressure pump, and the high-temperature condenser refrigerant liquid pipeline is connected to the outside. The steam generator refrigerant vapor channel is connected to the high-pressure steam inlet of the ejector, and the external refrigerant vapor channel is connected to the high-pressure steam inlet of the ejector, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0015] 9. The fourth type of heat-driven compression-ejection-absorption heat pump is defined in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in items 1-7, by eliminating the high-pressure pump and steam generator, eliminating the refrigerant liquid pipeline connecting the high-temperature condenser to the steam generator via the high-pressure pump, eliminating the refrigerant vapor channel connecting the steam generator to the high-pressure steam inlet of the ejector, and dividing the refrigerant vapor channel connecting the high-temperature condenser into two paths—the first path connecting the high-temperature condenser and the second path connecting the high-pressure steam inlet of the ejector, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0016] 10. The fourth type of heat-driven compression-ejection-absorption heat pump is defined in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in items 1-7, by eliminating the high-pressure pump and steam generator, eliminating the refrigerant liquid pipeline connecting the high-temperature condenser to the high-pressure pump and steam generator, eliminating the refrigerant vapor channel connecting the steam generator to the high-pressure steam inlet of the ejector, and dividing the refrigerant vapor channel connecting the expander into two paths—the first path connecting the expander and the second path connecting the high-pressure steam inlet of the ejector, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0017] 11. A fourth type of heat-driven compression-ejection-absorption heat pump is formed by adding a nozzle and replacing the throttle valve in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in items 1-10. Attached image description:

[0018] Figure 1 This is a schematic diagram of the first structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0019] Figure 2 This is a schematic diagram of the second structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0020] Figure 3 This is a schematic diagram of the third structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0021] Figure 4 This is a schematic diagram of the fourth type of thermally driven compression-ejection-absorption heat pump structure and process provided by the present invention.

[0022] Figure 5 This is a schematic diagram of the fifth structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0023] Figure 6 This is a schematic diagram of the sixth structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0024] Figure 7 This is a schematic diagram of the seventh structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0025] Figure 8 This is a schematic diagram of the eighth structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0026] Figure 9This is a schematic diagram of the ninth structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0027] Figure 10 This is a schematic diagram of the tenth structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0028] Figure 11 This is a schematic diagram of the 11th structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0029] Figure 12 This is a schematic diagram of the 12th structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0030] Figure 13 This is a schematic diagram of the 13th structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0031] Figure 14 This is a schematic diagram of the 14th structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0032] Figure 15 This is a schematic diagram of the 15th structure and process of the fourth type of heat-driven compression-ejection-absorption heat pump provided by the present invention.

[0033] In the diagram, 1-low temperature generator, 2-solution pump, 3-solution heat exchanger, 4-second solution heat exchanger, 5-high temperature generator, 6-absorber, 7-low temperature condenser, 8-low pressure pump, 9-evaporator, 10-compressor, 11-high temperature heat exchanger, 12-expander, 13-high temperature condenser, 14-throttle valve, 15-high pressure pump, 16-steam generator, 17-ejector, 18-regenerator, 19-second compressor, 20-second solution pump, 21-second absorber, A-nozzle. Detailed implementation method:

[0034] First, it should be noted that the structure and process are not repeated unless necessary; obvious processes are not described. The invention will now be described in detail with reference to the accompanying drawings and examples.

[0035] Figure 1 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0036] (1) Structurally, it mainly consists of a low-temperature generator, a solution pump, a solution heat exchanger, a second solution heat exchanger, a high-temperature generator, an absorber, a low-temperature condenser, a low-pressure pump, an evaporator, a compressor, a high-temperature heat exchanger, an expander, a high-temperature condenser, a throttle valve, a high-pressure pump, a steam generator, and an ejector; the low-temperature generator 1 has a concentrated solution pipeline connected to the high-temperature generator 5 via the solution pump 2, the solution heat exchanger 3, and the second solution heat exchanger 4; the high-temperature generator 5 also has a concentrated solution pipeline connected to the absorber 6 via the second solution heat exchanger 4; the absorber 6 also has a dilute solution pipeline connected to the low-temperature generator 1 via the solution heat exchanger 3; the low-temperature generator 1 also has a refrigerant vapor channel connected to the low-temperature condenser 7; the low-temperature condenser 7 also has a refrigerant liquid pipeline connected to the evaporator 9 via the low-pressure pump 8; the high-temperature generator 5 also has a refrigerant vapor channel connected to the compressor 10; the compressor 10 also has a refrigerant vapor channel connected to the compressor 10 via the high-temperature generator 5 via the high-temperature condenser 7 via the high-pressure pump 8, and the high-temperature generator 5 also has a refrigerant vapor channel connected to the compressor 10; the compressor 10 also has a refrigerant vapor channel connected to the high-temperature condenser 7 via the high-temperature condenser 7 via the high-pressure pump 8. The high-temperature heat exchanger 11 is connected to the expander 12. The expander 12 also has a refrigerant vapor channel connected to the high-temperature condenser 13. The high-temperature condenser 13 also has a refrigerant liquid pipeline connected to the evaporator 9 via the throttle valve 14. The high-temperature condenser 13 also has a refrigerant liquid pipeline connected to the steam generator 16 via the high-pressure pump 15. The steam generator 16 also has a refrigerant vapor channel connected to the high-pressure steam inlet of the ejector 17. The evaporator 9 also has a refrigerant vapor channel connected to the low-pressure steam inlet of the ejector 17. The ejector 17 also has a medium-pressure refrigerant vapor channel connected to the absorber 6. The high-temperature generator 5, the high-temperature heat exchanger 11, and the steam generator 16 also have high-temperature heat medium channels connected to the outside. The absorber 6 and the high-temperature condenser 13 also have heated medium channels connected to the outside. The low-temperature condenser 7 also has a cooling medium channel connected to the outside. The low-temperature generator 1 and the evaporator 9 also have low-temperature heat medium channels connected to the outside.

[0037] (2) In terms of process, the concentrated solution from the low-temperature generator 1 enters the high-temperature generator 5 via the solution pump 2, solution heat exchanger 3, and second solution heat exchanger 4. The high-temperature heat medium flows through the high-temperature generator 5, heating the solution inside and releasing refrigerant vapor, which is then supplied to the compressor 10. The concentrated solution from the high-temperature generator 5 enters the absorber 6 via the second solution heat exchanger 4, absorbing refrigerant vapor and releasing heat to the heated medium. The dilute solution from the absorber 6 enters the low-temperature generator 1 via the solution heat exchanger 3. The refrigerant liquid flows through the low-temperature generator 1, heating the solution inside and releasing refrigerant vapor. The refrigerant vapor in the low-temperature condenser 7 releases heat to the cooling medium to form a refrigerant liquid. The refrigerant liquid in the low-temperature condenser 7 is pressurized by the low-pressure pump 8 and enters the evaporator 9 to absorb heat and vaporize. The refrigerant vapor flows through the compressor 10 to increase its pressure and temperature, flows through the high-temperature heat exchanger 11 to absorb heat and increase its temperature, flows through the expander 12 to decrease its pressure and do work, and is then supplied to the high-temperature condenser 13. The refrigerant vapor entering the high-temperature condenser 13 releases heat to the heated medium to form a refrigerant liquid. The first stream of refrigerant liquid discharged from the high-temperature condenser 13 flows through the low-temperature generator 1 to release heat and decrease its temperature, and flows through the throttling valve 14 to decrease its pressure and temperature. The refrigerant liquid entering the evaporator 9 absorbs heat and vaporizes. The second stream of refrigerant liquid discharged from the high-temperature condenser 13 flows through the high-pressure pump 15 for pressurization and then enters the steam generator 16 for heat absorption, heating, and vaporization. The refrigerant steam discharged from the steam generator 16 is provided to the ejector 17 as working steam. The working steam enters the ejector 17, flows through the nozzles to reduce pressure and increase speed, and forms a low-pressure system. The refrigerant steam generated by the evaporator 9 is drawn into the low-pressure zone of the ejector 17. After the two streams of steam mix, they flow through the diffuser to reduce speed and increase pressure, forming medium-pressure steam, which is then supplied to the absorber 6. The high-temperature heat medium passes through the high-temperature generator 5 and the high-temperature heat... The heat exchanger 11 and the steam generator 16 provide high-temperature driving heat loads. The heated medium obtains medium-temperature heating loads through the absorber 6 and the high-temperature condenser 13. The low-temperature heat medium provides low-temperature heat loads through the evaporator 9. The cooling medium carries away the discharged cooling heat loads through the low-temperature condenser 7. The mechanical energy output by the expander 12 is used to power the compressor 10, or the mechanical energy output by the expander 12 is used to power the compressor 10 and the external environment, or the expander 12 and the external environment jointly provide power to the compressor 10, forming a fourth type of heat-driven compression-ejection-absorption heat pump.

[0038] Figure 2 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0039] (1) Structurally, in Figure 1In the fourth type of heat-driven compression-ejection-absorption heat pump shown, a regenerator 18 is added. The refrigerant vapor passage of the compressor 10 is connected to the expander 12 via the high-temperature heat exchanger 11. The refrigerant vapor passage of the compressor 10 is connected to the expander 12 via the regenerator 18 and the high-temperature heat exchanger 11. The refrigerant vapor passage of the expander 12 is connected to the high-temperature condenser 13 via the regenerator 18.

[0040] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant vapor discharged from the high-temperature generator 5 flows through the compressor 10 to increase its pressure and temperature, flows through the regenerator 18 and the high-temperature heat exchanger 11 to gradually absorb heat and increase its temperature, flows through the expander 12 to decrease its pressure and do work, flows through the regenerator 18 to release heat and decrease its temperature, and then supplies it to the high-temperature condenser 13, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0041] Figure 3 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0042] (1) Structurally, in Figure 1 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, a regenerator 18 is added. The refrigerant vapor passage of the compressor 10 is connected to the expander 12 through the high-temperature heat exchanger 11. The compressor 10 is then connected to itself through the regenerator 18. After that, the compressor 10 has a refrigerant vapor passage connected to the expander 12 through the high-temperature heat exchanger 11. The refrigerant vapor passage of the expander 12 is connected to the high-temperature condenser 13. The expander 12 has a refrigerant vapor passage connected to the high-temperature condenser 13 through the regenerator 18.

[0043] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that: the refrigerant vapor discharged from the high-temperature generator 5 enters the compressor 10 to increase its pressure and temperature. After reaching a certain level, it flows through the regenerator 18 to absorb heat and increase its temperature, and then enters the compressor 10 to continue to increase its pressure and temperature; the refrigerant vapor discharged from the compressor 10 flows through the high-temperature heat exchanger 11 to absorb heat and increase its temperature, flows through the expander 12 to reduce its pressure and do work, flows through the regenerator 18 to release heat and decrease its temperature, and then supplies it to the high-temperature condenser 13, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0044] Figure 4 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0045] (1) Structurally, in Figure 1In the fourth type of heat-driven compression-ejection-absorption heat pump shown, a regenerator 18 is added. The refrigerant vapor passage of the compressor 10 is connected to the expander 12 via the high-temperature heat exchanger 11. The refrigerant vapor passage of the compressor 10 is then connected to the expander 12 via the regenerator 18 and the high-temperature heat exchanger 11. The refrigerant vapor passage of the expander 12 is then connected to the high-temperature condenser 13. The refrigerant vapor passage of the expander 12 is then connected to itself via the regenerator 18, and then the expander 12 has a refrigerant vapor passage connected to the high-temperature condenser 13.

[0046] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that: the refrigerant vapor discharged from the high-temperature generator 5 flows through the compressor 10 to increase its pressure and temperature, flows through the regenerator 18 and the high-temperature heat exchanger 11 to gradually absorb heat and increase its temperature, and then supplies it to the expander 12; the refrigerant vapor enters the expander 12 to reduce its pressure and do work, and after reaching a certain level, it flows through the regenerator 18 to release heat and reduce its temperature, enters the expander 12 to continue to reduce its pressure and do work, and then supplies it to the high-temperature condenser 13, forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0047] Figure 5 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0048] (1) Structurally, in Figure 1 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, a regenerator 18 and a second compressor 19 are added. The compressor 10 is adjusted so that the refrigerant vapor passage is connected to the expander 12 via the high-temperature heat exchanger 11. The compressor 10 is connected to the expander 12 via the regenerator 18 and the high-temperature heat exchanger 11. An intermediate extraction steam passage is added to the expander 12, which is connected to the second compressor 19 via the regenerator 18. The second compressor 19 is also connected to the expander 12 via the high-temperature heat exchanger 11. The expander 12 connects the compressor 10 and the second compressor 19 and transmits power.

[0049] (2) In terms of process, with Figure 1Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference lies in the following: the refrigerant vapor discharged from the high-temperature generator 5 flows through the compressor 10 to increase its pressure and temperature, then flows through the regenerator 18 and the high-temperature heat exchanger 11 to gradually absorb heat and increase its temperature, and then supplies it to the expander 12; the refrigerant vapor discharged from the second compressor 19 flows through the high-temperature heat exchanger 11 to absorb heat and increase its temperature, and then supplies it to the expander 12; the refrigerant vapor enters the expander 12 to reduce its pressure and do work, and after a certain degree, it splits into two paths - the first path flows through the regenerator 18 to release heat and reduce its temperature, and then enters the second compressor 19 to increase its pressure and temperature, and the second path continues to reduce its pressure and do work before supplying it to the high-temperature condenser 13; the mechanical energy output by the expander 12 provides power to the compressor 10 and the second compressor 19, or the mechanical energy output by the expander 12 provides power to the compressor 10, the second compressor 19 and the outside, or the expander 12 and the outside jointly provide power to the compressor 10 and the second compressor 19, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0050] Figure 6 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0051] (1) Structurally, in Figure 1 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, a second solution pump 20 is added. The low-temperature generator 1 is connected to the high-temperature generator 5 via a concentrated solution pipeline through solution pump 2, solution heat exchanger 3, and second solution heat exchanger 4. The connection is adjusted so that the low-temperature generator 1 is connected to the absorber 6 via a concentrated solution pipeline through the second solution pump 20 and second solution heat exchanger 4. The absorber 6 is then connected to the high-temperature generator 5 via a dilute solution pipeline through solution pump 2 and solution heat exchanger 3. The high-temperature generator 5 is connected to the absorber 6 via a concentrated solution pipeline through the second solution heat exchanger 4. The connection is adjusted so that the high-temperature generator 5 is connected to the low-temperature generator 1 via a concentrated solution pipeline through solution heat exchanger 3 and second solution heat exchanger 4.

[0052] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference lies in the following: the dilute solution of absorber 6 enters high-temperature generator 5 via solution pump 2 and solution heat exchanger 3. The high-temperature heat medium flows through high-temperature generator 5, heats the solution inside, releases refrigerant vapor, and supplies it to compressor 10. The concentrated solution of high-temperature generator 5 enters low-temperature generator 1 via solution heat exchanger 3 and second solution heat exchanger 4. The refrigerant liquid flows through low-temperature generator 1, heats the solution inside, releases refrigerant vapor, and supplies it to low-temperature condenser 7. The concentrated solution of low-temperature generator 1 enters absorber 6 via second solution pump 20 and second solution heat exchanger 4, absorbs refrigerant vapor, and releases heat to the heated medium, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0053] Figure 7The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0054] (1) Structurally, in Figure 1 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the low-temperature condenser 7 and its cooling medium channel connected to the outside are removed, the low-pressure pump 8 is removed, and the refrigerant liquid pipeline connecting the low-temperature condenser 7 to the evaporator 9 via the low-pressure pump 8 is removed; a second solution pump 20 and a second absorber 21 are added, and the connection between the concentrated solution pipeline of the low-temperature generator 1 and the high-temperature generator 5 via the solution pump 2, solution heat exchanger 3 and the second solution heat exchanger 4 is adjusted so that the concentrated solution pipeline of the low-temperature generator 1 is connected to the absorber 6 via the second solution pump 20 and solution heat exchanger 3, and the absorber 6 also has a dilute solution pipeline. The solution heat exchanger 3 is connected to the second absorber 21. The second absorber 21 then has a dilute solution pipeline connected to the solution pump 2 and the second solution heat exchanger 4, and a high-temperature generator 5. The high-temperature generator 5 is then connected to the absorber 6 via the second solution heat exchanger 4, and the high-temperature generator 5 is then connected to the low-temperature generator 1 via the second solution heat exchanger 4. The low-temperature generator 1 is then connected to the low-temperature condenser 7 via a refrigerant vapor channel, and the low-temperature generator 1 is then connected to the second absorber 21 via a refrigerant vapor channel. The second absorber 21 also has a cooling medium channel connected to the outside.

[0055] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference lies in the following: the dilute solution of absorber 6 enters the second absorber 21 via solution heat exchanger 3, absorbs refrigerant vapor and releases heat to the cooling medium; the dilute solution of the second absorber 21 enters the high-temperature generator 5 via solution pump 2 and second solution heat exchanger 4; the high-temperature heat medium flows through the high-temperature generator 5, heats the solution inside, releases refrigerant vapor and enters the compressor 10 to increase pressure and temperature; the concentrated solution of the high-temperature generator 5 enters the low-temperature generator 1 via the second solution heat exchanger 4; the refrigerant liquid flows through the low-temperature generator 1, heats the solution inside, releases refrigerant vapor and provides it to the second absorber 21; the concentrated solution of the low-temperature generator 1 enters the absorber 6 via the second solution pump 20 and solution heat exchanger 3, absorbs refrigerant vapor and releases heat to the heated medium, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0056] Figure 8 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0057] (1) Structurally, in Figure 1In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are removed. The high-temperature condenser 11 is connected to the steam generator 16 via the high-pressure pump 15, and the high-temperature condenser 11 is connected to the outside via the refrigerant liquid pipeline. The steam generator 16 is connected to the high-pressure steam inlet of the ejector 10 via the refrigerant steam channel, and the external working steam channel is connected to the high-pressure steam inlet of the ejector 10.

[0058] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 13 is divided into two paths: the first path flows through the low-temperature generator 1 to release heat and cool down, flows through the throttling valve 14 to reduce pressure and cool down, and enters the evaporator 9 to absorb heat and vaporize; the second path is discharged to the outside; working steam is provided to the ejector 17 from the outside, forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0059] Figure 9 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0060] (1) Structurally, in Figure 6 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are removed. The high-temperature condenser 11 is connected to the steam generator 16 via the high-pressure pump 15, and the high-temperature condenser 11 is connected to the outside via the refrigerant liquid pipeline. The steam generator 16 is connected to the high-pressure steam inlet of the ejector 10 via the refrigerant steam channel, and the external working steam channel is connected to the high-pressure steam inlet of the ejector 10.

[0061] (2) In terms of process, with Figure 6 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 13 is divided into two paths: the first path flows through the low-temperature generator 1 to release heat and cool down, flows through the throttling valve 14 to reduce pressure and cool down, and enters the evaporator 9 to absorb heat and vaporize; the second path is discharged to the outside; working steam is provided to the ejector 17 from the outside, forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0062] Figure 10 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0063] (1) Structurally, in Figure 7In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are removed. The high-temperature condenser 11 is connected to the steam generator 16 via the high-pressure pump 15, and the high-temperature condenser 11 is connected to the outside via the refrigerant liquid pipeline. The steam generator 16 is connected to the high-pressure steam inlet of the ejector 10 via the refrigerant steam channel, and the external working steam channel is connected to the high-pressure steam inlet of the ejector 10.

[0064] (2) In terms of process, with Figure 7 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 13 is divided into two paths: the first path flows through the low-temperature generator 1 to release heat and cool down, flows through the throttling valve 14 to reduce pressure and cool down, and enters the evaporator 9 to absorb heat and vaporize; the second path is discharged to the outside; working steam is provided to the ejector 17 from the outside, forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0065] Figure 11 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0066] (1) Structurally, in Figure 1 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are eliminated, the refrigerant liquid pipeline connecting the high-temperature condenser 13 to the steam generator 16 via the high-pressure pump 15 is eliminated, the refrigerant vapor channel connecting the steam generator 16 to the high-pressure steam inlet of the ejector 17 is eliminated, and the refrigerant vapor channel connecting the high-temperature condenser 13 is divided into two paths—the first path connects to the high-temperature condenser 13 and the second path connects to the high-pressure steam inlet of the ejector 17.

[0067] (2) In terms of process, with Figure 1 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant vapor discharged from the expander 12 is divided into two paths - the first path enters the high-temperature condenser 13 to release heat and condense, and the second path enters the ejector 17 to reduce pressure and increase speed, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0068] Figure 12 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0069] (1) Structurally, in Figure 6In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are eliminated, the refrigerant liquid pipeline connecting the high-temperature condenser 13 to the steam generator 16 via the high-pressure pump 15 is eliminated, the refrigerant vapor channel connecting the steam generator 16 to the high-pressure steam inlet of the ejector 17 is eliminated, and the refrigerant vapor channel connecting the high-temperature condenser 13 is divided into two paths—the first path connects to the high-temperature condenser 13 and the second path connects to the high-pressure steam inlet of the ejector 17.

[0070] (2) In terms of process, with Figure 6 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant vapor discharged from the expander 12 is divided into two paths—the first path enters the high-temperature condenser 13 to release heat and condense, and the second path enters the ejector 17 to reduce pressure and increase speed, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0071] Figure 13 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0072] (1) Structurally, in Figure 7 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are eliminated, the refrigerant liquid pipeline connecting the high-temperature condenser 13 to the steam generator 16 via the high-pressure pump 15 is eliminated, the refrigerant vapor channel connecting the steam generator 16 to the high-pressure steam inlet of the ejector 17 is eliminated, and the refrigerant vapor channel connecting the high-temperature condenser 13 is divided into two paths—the first path connects to the high-temperature condenser 13 and the second path connects to the high-pressure steam inlet of the ejector 17.

[0073] (2) In terms of process, with Figure 7 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant vapor discharged from the expander 12 is divided into two paths - the first path enters the high-temperature condenser 13 to release heat and condense, and the second path enters the ejector 17 to reduce pressure and increase speed, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0074] Figure 14 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0075] (1) Structurally, in Figure 1 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, the high-pressure pump 15 and the steam generator 16 are eliminated, the refrigerant liquid pipeline connecting the high-temperature condenser 13 to the steam generator 16 via the high-pressure pump 15 is eliminated, the refrigerant vapor channel connecting the steam generator 16 to the high-pressure steam inlet of the ejector 17 is eliminated, and the refrigerant vapor channel connecting the expander 12 is divided into two paths—the first path connects to the expander 12 and the second path connects to the high-pressure steam inlet of the ejector 17.

[0076] (2) In terms of process, with Figure 1 Compared with the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant vapor emitted by the high-temperature heat exchanger 11 is divided into two paths - the first path enters the expander 12 to reduce pressure and do work, and the second path enters the ejector 17 to reduce pressure and increase speed, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0077] Figure 15 The fourth type of heat-driven compression-ejection-absorption heat pump shown is implemented as follows:

[0078] (1) Structurally, in Figure 7 In the fourth type of heat-driven compression-ejection-absorption heat pump shown, nozzle A is added and throttle valve 14 is replaced.

[0079] (2) In terms of process, with Figure 7 Compared to the fourth type of heat-driven compression-ejection-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 13 is divided into two paths: the first path flows through the low-temperature generator 1 to release heat and cool down, flows through the nozzle A to reduce pressure and increase speed, and enters the evaporator 9 to absorb heat and vaporize; the second path is pressurized by the high-pressure pump 15 and then enters the steam generator 16 to absorb heat, increase temperature, and vaporize, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

[0080] The effects achievable by this invention—the fourth type of heat-driven compression-ejection-absorption heat pump proposed in this invention has the following effects and advantages:

[0081] (1) New technologies for heating driven by thermal energy or by a combination of thermal and mechanical energy have been proposed, enriching the cooling / heating technology.

[0082] (2) Thermal energy-driven combined cooling and heating, or combined cooling and heating technologies are proposed, which have a wide range of energy supply and can meet different types of energy needs.

[0083] (3) Effectively improves the working parameters of refrigerant vapor, significantly expands the working range of heat pump, and is conducive to achieving a larger temperature span for cooling / heating.

[0084] (4) The process is reasonable and the performance index is reasonable; the structure is simple and the manufacturing cost is reduced.

[0085] (5) It is conducive to the full utilization of energy of different grades and types, and to reducing the irreversible loss of systemic temperature difference.

[0086] (6) The ejector is simple to manufacture, durable, and has little irreversible loss, which is beneficial to improving the performance index of the heat pump.

[0087] (7) It can significantly increase the heating temperature, making up for the shortcomings of absorption heat pump technology and effectively avoiding the conflict between the parameters of the driving heat medium and the performance of the solution.

[0088] (8) It provides a variety of specific technical solutions, which can cope with many different actual situations and has a wide range of applications. It is conducive to expanding the application scope and value of the fourth type of heat-driven compression-jet-absorption heat pump technology.

Claims

1. The fourth type of heat-driven compression-ejection-absorption heat pump mainly consists of a low-temperature generator, a solution pump, a solution heat exchanger, a second solution heat exchanger, a high-temperature generator, an absorber, a low-temperature condenser, a low-pressure pump, an evaporator, a compressor, a high-temperature heat exchanger, an expander, a high-temperature condenser, a throttle valve, a high-pressure pump, a steam generator, and an ejector; the low-temperature generator (1) has a concentrated solution pipeline connected to the high-temperature generator (5) via the solution pump (2), the solution heat exchanger (3), and the second solution heat exchanger (4); the high-temperature generator ( 5) The concentrated solution pipeline is connected to the absorber (6) via the second solution heat exchanger (4). The absorber (6) is also connected to the low-temperature generator (1) via the solution heat exchanger (3). The low-temperature generator (1) is also connected to the low-temperature condenser (7) via the refrigerant vapor channel. The low-temperature condenser (7) is also connected to the evaporator (9) via the low-pressure pump (8). The high-temperature generator (5) is also connected to the compressor (10) via the refrigerant vapor channel. The compressor (10) is also connected to the high-temperature heat exchanger (1) via the high-temperature heat exchanger (1) 1) It is connected to the expander (12). The expander (12) is also connected to the high-temperature condenser (13) via a refrigerant vapor passage. The high-temperature condenser (13) is also connected to the evaporator (9) via a refrigerant liquid pipeline through a low-temperature generator (1) and a throttle valve (14). The high-temperature condenser (13) is also connected to the steam generator (16) via a high-pressure pump (15). The steam generator (16) is also connected to the high-pressure steam inlet of the ejector (17) via a refrigerant vapor passage. The evaporator (9) is also connected to the ejector (17) via a refrigerant vapor passage. The low-pressure steam inlet, the ejector (17) and the medium-pressure refrigerant steam channel are connected to the absorber (6), the high-temperature generator (5), the high-temperature heat exchanger (11) and the steam generator (16) are connected to the outside through high-temperature heat medium channels, the absorber (6) and the high-temperature condenser (13) are connected to the outside through heated medium channels, the low-temperature condenser (7) is connected to the outside through cooling medium channels, and the evaporator (9) is connected to the outside through low-temperature heat medium channels, forming a fourth type of heat-driven compression-ejection-absorption heat pump.

2. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in claim 1, with the addition of a regenerator (18), the compressor (10) having a refrigerant vapor passage connected to the expander (12) via the high-temperature heat exchanger (11) is adjusted so that the compressor (10) has a refrigerant vapor passage connected to the expander (12) via the regenerator (18) and the high-temperature heat exchanger (11), and the expander (12) having a refrigerant vapor passage connected to the high-temperature condenser (13) is adjusted so that the expander (12) has a refrigerant vapor passage connected to the high-temperature condenser (13) via the regenerator (18), thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

3. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in claim 1, with the addition of a regenerator (18). The compressor (10) is connected to the expander (12) via a refrigerant vapor channel through a high-temperature heat exchanger (11). The compressor (10) is then connected to itself via the regenerator (18). After that, the compressor (10) is connected to the expander (12) via a refrigerant vapor channel through a high-temperature heat exchanger (11). The expander (12) is connected to the high-temperature condenser (13) via a refrigerant vapor channel through the regenerator (18). This forms the fourth type of heat-driven compression-ejection-absorption heat pump.

4. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in claim 1, with the addition of a regenerator (18). The compressor (10) is connected to the expander (12) via a refrigerant vapor channel through a high-temperature heat exchanger (11). The compressor (10) is then connected to the expander (12) via a regenerator vapor channel through the regenerator (18) and the high-temperature heat exchanger (11). The expander (12) is connected to the high-temperature condenser (13) via a refrigerant vapor channel through the regenerator (18) and then to the expander (12) itself. The expander (12) is then connected to the high-temperature condenser (13) via a refrigerant vapor channel through the regenerator (18). This forms the fourth type of heat-driven compression-ejection-absorption heat pump.

5. The fourth type of heat-driven compression-ejection-absorption heat pump is the fourth type of heat-driven compression-ejection-absorption heat pump described in claim 1, with the addition of a regenerator (18) and a second compressor (19). The compressor (10) is adjusted so that the refrigerant vapor passage is connected to the expander (12) through the high-temperature heat exchanger (11), and the compressor (10) has a refrigerant vapor passage connected to the expander (12) through the regenerator (18) and the high-temperature heat exchanger (11). The expander (12) is provided with an intermediate extraction steam passage connected to the second compressor (19) through the regenerator (18). The second compressor (19) also has a refrigerant vapor passage connected to the expander (12) through the high-temperature heat exchanger (11). The expander (12) connects the compressor (10) and the second compressor (19) and transmits power, thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

6. The fourth type of heat-driven compression-ejection-absorption heat pump is made by adding a second solution pump (20) to any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in claims 1-5. The low-temperature generator (1) is connected to the high-temperature generator (5) via a concentrated solution pipeline through the solution pump (2), the solution heat exchanger (3), and the second solution heat exchanger (4). The connection is adjusted so that the low-temperature generator (1) is connected to the absorber (6) via a concentrated solution pipeline through the second solution pump (20) and the second solution heat exchanger (4). The absorber (6) is then connected to the high-temperature generator (5) via a dilute solution pipeline through the solution pump (2) and the solution heat exchanger (3). The connection is adjusted so that the high-temperature generator (5) is connected to the absorber (6) via a concentrated solution pipeline through the second solution heat exchanger (4) and the second solution heat exchanger (4). The connection is adjusted so that the high-temperature generator (5) is connected to the low-temperature generator (1) via a concentrated solution pipeline through the solution heat exchanger (3) and the second solution heat exchanger (4).

7. The fourth type of heat-driven compression-ejection-absorption heat pump is, in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in claims 1-5, wherein the low-temperature condenser (7) and its cooling medium channel connected to the outside are removed, the low-pressure pump (8) is removed, and the refrigerant liquid pipeline connecting the low-temperature condenser (7) to the evaporator (9) via the low-pressure pump (8) is removed; a second solution pump (20) and a second absorber (21) are added, and the connection between the concentrated solution pipeline of the low-temperature generator (1) and the high-temperature generator (5) via the solution pump (2), the solution heat exchanger (3), and the second solution heat exchanger (4) is adjusted so that the concentrated solution pipeline of the low-temperature generator (1) is connected to the absorber (6) via the second solution pump (20) and the solution heat exchanger (3), and the absorber (6) is also A dilute solution pipeline is connected to the second absorber (21) via a solution heat exchanger (3). The second absorber (21) is then connected to the high-temperature generator (5) via a solution pump (2) and the second solution heat exchanger (4). The high-temperature generator (5) is then connected to the absorber (6) via a concentrated solution pipeline via the second solution heat exchanger (4). The high-temperature generator (5) is then connected to the low-temperature generator (1) via a concentrated solution pipeline via the second solution heat exchanger (4). The low-temperature generator (1) is then connected to the low-temperature condenser (7) via a refrigerant vapor channel. The low-temperature generator (1) is then connected to the second absorber (21) via a refrigerant vapor channel. The second absorber (21) also has a cooling medium channel connected to the outside, forming a fourth type of heat-driven compression-ejection-absorption heat pump.

8. The fourth type of heat-driven compression-ejection-absorption heat pump is formed by eliminating the high-pressure pump (15) and the steam generator (16) in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in claims 1-7, adjusting the high-temperature condenser (11) to have a refrigerant liquid pipeline connected to the steam generator (16) via the high-pressure pump (15), and adjusting the high-temperature condenser (11) to have a refrigerant liquid pipeline connected to the outside, and adjusting the steam generator (16) to have a refrigerant vapor channel connected to the high-pressure steam inlet of the ejector (10), and adjusting the external refrigerant vapor channel connected to the high-pressure steam inlet of the ejector (10), thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

9. The fourth type of heat-driven compression-ejection-absorption heat pump is, in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in claims 1-7, the high-pressure pump (15) and the steam generator (16) are removed, the refrigerant liquid pipeline connecting the high-temperature condenser (13) to the steam generator (16) via the high-pressure pump (15) is removed, the refrigerant vapor channel connecting the steam generator (16) to the high-pressure steam inlet of the ejector (17) is removed, and the refrigerant vapor channel connecting the high-temperature condenser (13) is divided into two paths - the first path connects to the high-temperature condenser (13) and the second path connects to the high-pressure steam inlet of the ejector (17), thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

10. The fourth type of heat-driven compression-ejection-absorption heat pump is formed by eliminating the high-pressure pump (15) and the steam generator (16) in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in claims 1-7, eliminating the refrigerant liquid pipeline connecting the high-temperature condenser (13) to the steam generator (16) via the high-pressure pump (15), eliminating the refrigerant vapor channel connecting the steam generator (16) to the high-pressure steam inlet of the ejector (17), and dividing the refrigerant vapor channel connecting the expander (12) into two paths—the first path connecting the expander (12) and the second path connecting the high-pressure steam inlet of the ejector (17), thus forming the fourth type of heat-driven compression-ejection-absorption heat pump.

11. A fourth type of heat-driven compression-ejection-absorption heat pump is formed by adding a nozzle (A) and replacing the throttle valve (14) in any of the fourth type of heat-driven compression-ejection-absorption heat pumps described in claims 1-10.

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