Fourth type injection-absorption heat pump
By designing a fourth type of jet-absorption heat pump, which combines the advantages of ejectors and absorption heat pumps, the problem of low thermal energy utilization efficiency in existing technologies is solved, achieving efficient and low-cost cooling/heating effects.
Patent Information
- Application Number
- CN202511650463.7
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Priority Date
- 2024-11-12
- Filing Date
- 2025-10-31
- Publication Date
- 2026-02-24
Smart Images

Figure CN121557636A_ABST
Abstract
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] The ejector itself is a pressure boosting component, which has the advantages of simple structure, reliable operation, low investment and long service life; more importantly, the ejector can effectively adapt to high temperature heat loads - for heat pump systems, this is conducive to improving the rationalization of the driving heat load input link and expanding the utilization range of heat pump technology for high temperature heat loads.
[0004] Among technologies that utilize thermal energy for cooling / heating, absorption cooling / 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 due to the properties of the solution and refrigerant medium.
[0005] Based on the principles of simple, proactive, and efficient utilization of thermal energy for cooling / heating, this invention proposes a fourth type of jet-absorption heat pump with a reasonable process, simple structure, low cost, wide operating range, and rationalized performance index, achieving technological integration. Summary of the Invention:
[0006] The main objective of this invention is to provide a fourth type of jet-absorption heat pump, the specific contents of which are described below:
[0007] 1. The fourth type of jet-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 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 high-temperature evaporator. The condenser is connected, and the high-temperature condenser is connected to the low-temperature generator via a refrigerant liquid line. The low-temperature generator is then connected to the evaporator via a refrigerant liquid line through a throttling valve. The high-temperature condenser is also connected to the steam generator via a refrigerant liquid line through a high-pressure pump. The steam generator is connected to the high-pressure steam inlet of the ejector via a refrigerant steam channel. The evaporator is also connected to the low-pressure steam inlet of the ejector via a refrigerant steam channel. The ejector is connected to the absorber via a medium-pressure refrigerant steam channel. The high-temperature generator and the steam generator are also connected to the outside via high-temperature heat medium channels. The absorber and the high-temperature condenser are also connected to the outside via heated medium channels. The low-temperature condenser is connected to the outside via a cooling medium channel. The evaporator is connected to the outside via a low-temperature heat medium channel, forming the fourth type of jet-absorption heat pump.
[0008] 2. The fourth type of jet-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 high-temperature condenser, a throttling valve, 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 passage 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 passage... The system connects to the high-temperature condenser, which in turn connects to the low-temperature generator via a refrigerant liquid line. The low-temperature generator then connects to the evaporator via a refrigerant liquid line through a throttling valve. The high-temperature condenser also connects to the outside via a refrigerant liquid line. The outside has a working steam channel connecting to the high-pressure steam inlet of the ejector. The evaporator also has a refrigerant steam channel connecting to the low-pressure steam inlet of the ejector. The ejector also has a medium-pressure refrigerant steam channel connecting to the absorber. The high-temperature generator also has a high-temperature heat medium channel connecting to the outside. The absorber and high-temperature condenser each have a heated medium channel connecting to the outside. The low-temperature condenser also has a cooling medium channel connecting to the outside. The evaporator also has a low-temperature heat medium channel connecting to the outside, forming the fourth type of jet-absorption heat pump.
[0009] 3. The fourth type of jet-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 high-temperature condenser, a throttling valve, 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… There is also a refrigerant vapor channel connected to the high-temperature condenser. The high-temperature condenser is connected to the low-temperature generator via a refrigerant liquid line. The low-temperature generator is then connected to the evaporator via a refrigerant liquid line through a throttling valve. The high-temperature generator is also connected to the high-pressure steam inlet of the ejector via a refrigerant vapor channel. The evaporator is also connected to the low-pressure steam inlet of the ejector via a refrigerant vapor channel. The ejector is also connected to the absorber via a medium-pressure refrigerant vapor channel. The high-temperature generator is also connected to the outside via a high-temperature heat medium channel. The absorber and the high-temperature condenser are also connected to the outside via heated medium channels. The low-temperature condenser is also connected to the outside via a cooling medium channel. The evaporator is also connected to the outside via a low-temperature heat medium channel, forming the fourth type of jet-absorption heat pump.
[0010] 4. The fourth type of jet-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 high-temperature condenser, a throttling valve, a high-pressure pump, a steam generator, an ejector, and a second solution pump. The absorber has a dilute solution pipeline connected to the high-temperature generator via the solution pump and the solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the low-temperature generator via the solution heat exchanger and the second solution heat exchanger. The low-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution pump and the second 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. The steam channel is connected to the high-temperature condenser. The high-temperature condenser also has a refrigerant liquid line connected to the low-temperature generator. The low-temperature generator then has a refrigerant liquid line connected to the evaporator via a throttling valve. The high-temperature condenser also has a refrigerant liquid line connected to the steam generator via a high-pressure pump. The steam generator also has a refrigerant steam channel connected to the high-pressure steam inlet of the ejector. The evaporator also has a refrigerant steam channel connected to the low-pressure steam inlet of the ejector. The ejector also has a medium-pressure refrigerant steam channel connected to the absorber. The high-temperature generator and the steam generator also have high-temperature heat medium channels connected to the outside. The absorber and the 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 the fourth type of jet-absorption heat pump.
[0011] 5. The fourth type of jet-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 high-temperature condenser, a throttling valve, an ejector, and a second solution pump. The absorber has a dilute solution pipeline connected to the high-temperature generator via the solution pump and the solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the low-temperature generator via the solution heat exchanger and the second solution heat exchanger. The low-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution pump and the second 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... There is a refrigerant vapor channel connected to the high-temperature condenser. The high-temperature condenser also has a refrigerant liquid line connected to the low-temperature generator. The low-temperature generator then has a refrigerant liquid line connected to the evaporator via a throttling valve. The high-temperature condenser also has a refrigerant liquid line connected to the outside. The outside has a working steam 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 also has a high-temperature heat medium channel connected to the outside. The absorber and the 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 the fourth type of jet-absorption heat pump.
[0012] 6. The fourth type of jet-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 high-temperature condenser, a throttling valve, an ejector, and a second solution pump. The absorber has a dilute solution pipeline connected to the high-temperature generator via the solution pump and the solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the low-temperature generator via the solution heat exchanger and the second solution heat exchanger. The low-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution pump and the second 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 high-temperature condenser. The high-temperature condenser also has a refrigerant liquid line connected to the low-temperature generator. The low-temperature generator then has a refrigerant liquid line connected to the evaporator via a throttling valve. The high-temperature 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 also has a high-temperature heat medium channel connected to the outside. The absorber and the 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 the fourth type of jet-absorption heat pump.
[0013] 7. The fourth type of jet-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, an evaporator, a high-temperature condenser, a throttling valve, a high-pressure pump, a steam generator, an ejector, a second solution pump, and a second absorber. The absorber has a dilute solution pipeline connected to the second absorber via the solution heat exchanger. The second absorber also has a dilute solution pipeline connected to the high-temperature generator via the solution pump and the second solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the low-temperature generator via the second solution heat exchanger. The low-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution pump and the solution heat exchanger. The low-temperature generator also has a refrigerant vapor channel connected to the second absorber, and the high-temperature generator also has a refrigerant vapor channel. The system is connected to a high-temperature condenser, which in turn has a refrigerant liquid line connected to a low-temperature generator. The low-temperature generator then has a refrigerant liquid line connected to an evaporator via a throttling valve. The high-temperature condenser also has a refrigerant liquid line connected to a steam generator via a high-pressure pump. The steam generator 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 and the steam generator each have a high-temperature heat medium channel connected to the outside. The absorber and the high-temperature condenser each have a heated medium channel connected to the outside. The evaporator also has a low-temperature heat medium channel connected to the outside. The second absorber also has a cooling medium channel connected to the outside, forming a fourth type of jet-absorption heat pump.
[0014] 8. The fourth type of jet-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, an evaporator, a high-temperature condenser, a throttling valve, an ejector, a second solution pump, and a second absorber. The absorber has a dilute solution pipeline connected to the second absorber via the solution heat exchanger. The second absorber also has a dilute solution pipeline connected to the high-temperature generator via the solution pump and the second solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the low-temperature generator via the second solution heat exchanger. The low-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution pump and the solution heat exchanger. The low-temperature generator also has a refrigerant vapor channel connected to the second absorber. The high-temperature generator also has a refrigerant vapor channel. The steam channel is connected to the high-temperature condenser. The high-temperature condenser also has a refrigerant liquid line connected to the low-temperature generator. The low-temperature generator then has a refrigerant liquid line connected to the evaporator via a throttling valve. The high-temperature condenser also has a refrigerant liquid line connected to the outside. The outside has a working steam channel connected to the high-pressure steam inlet of the ejector. The evaporator also has a refrigerant steam channel connected to the low-pressure steam inlet of the ejector. The ejector also has a medium-pressure refrigerant steam channel connected to the absorber. The high-temperature generator also has a high-temperature heat medium channel connected to the outside. The absorber and the high-temperature condenser also have heated medium channels connected to the outside. The evaporator also has a low-temperature heat medium channel connected to the outside. The second absorber also has a cooling medium channel connected to the outside, forming the fourth type of jet-absorption heat pump.
[0015] 9. The fourth type of jet-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, an evaporator, a high-temperature condenser, a throttling valve, an ejector, a second solution pump, and a second absorber. The absorber has a dilute solution pipeline connected to the second absorber via the solution heat exchanger. The second absorber also has a dilute solution pipeline connected to the high-temperature generator via the solution pump and the second solution heat exchanger. The high-temperature generator also has a concentrated solution pipeline connected to the low-temperature generator via the second solution heat exchanger. The low-temperature generator also has a concentrated solution pipeline connected to the absorber via the second solution pump and the solution heat exchanger. The low-temperature generator also has a refrigerant vapor channel connected to the second absorber. The generator also has a refrigerant vapor channel connected to the high-temperature condenser. The high-temperature condenser has a refrigerant liquid line connected to the low-temperature generator. The low-temperature generator then has a refrigerant liquid line connected to the evaporator via a throttling valve. The high-temperature 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 also has a high-temperature heat medium channel connected to the outside. The absorber and the high-temperature condenser also have heated medium channels connected to the outside. The evaporator also has a low-temperature heat medium channel connected to the outside. The second absorber also has a cooling medium channel connected to the outside, forming a fourth type of jet-absorption heat pump.
[0016] 10. A fourth type of jet-absorption heat pump is formed by adding a nozzle and replacing the throttle valve in any of the fourth type of jet-absorption heat pumps described in items 1-9. Attached image description:
[0017] Figure 1 This is a schematic diagram of the first structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0018] Figure 2 This is a schematic diagram of the second structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0019] Figure 3 This is a schematic diagram of the third structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0020] Figure 4 This is a schematic diagram of the fourth type of structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0021] Figure 5 This is a schematic diagram of the fifth structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0022] Figure 6 This is a schematic diagram of the sixth structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0023] Figure 7 This is a schematic diagram of the seventh structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0024] Figure 8 This is a schematic diagram of the eighth structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0025] Figure 9 This is a schematic diagram of the ninth structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0026] Figure 10 This is a schematic diagram of the tenth structure and process of the fourth type of jet-absorption heat pump provided by the present invention.
[0027] 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-high temperature condenser, 11-throttle valve, 12-high pressure pump, 13-steam generator, 14-ejector, 15-second solution pump, 16-second absorber, A-nozzle. Detailed implementation method:
[0028] 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.
[0029] Figure 1 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0030] (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 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; and the high-temperature generator 5 also has a refrigerant vapor channel connected to the high-temperature condenser 1. The high-temperature condenser 10 is connected to the low-temperature generator 1 via a refrigerant liquid pipeline. The low-temperature generator 1 is then connected to the evaporator 9 via a refrigerant liquid pipeline through a throttle valve 11. The high-temperature condenser 10 is also connected to the steam generator 13 via a refrigerant liquid pipeline through a high-pressure pump 12. The steam generator 13 is also connected to the high-pressure steam inlet of the ejector 14 via a refrigerant steam channel. The evaporator 9 is also connected to the low-pressure steam inlet of the ejector 14 via a refrigerant steam channel. The ejector 14 is also connected to the absorber 6 via a medium-pressure refrigerant steam channel. The high-temperature generator 5 and the steam generator 13 are also connected to the outside via high-temperature heat medium channels. The absorber 6 and the high-temperature condenser 10 are also connected to the outside via heated medium channels. The low-temperature condenser 7 is connected to the outside via a cooling medium channel. The evaporator 9 is also connected to the outside via a low-temperature heat medium channel.
[0031] (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 high-temperature condenser 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, absorbing heat and releasing refrigerant vapor, which is then supplied to the low-temperature condenser 7. The refrigerant vapor from the low-temperature condenser 7 releases heat to the cooling medium to form refrigerant liquid. The refrigerant liquid from 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 from the high-temperature condenser 10 releases heat to the heated medium to form refrigerant liquid. The first path of refrigerant liquid discharged from the high-temperature condenser 10 flows through the generator 1 to release heat and cool down, and then flows through the throttling valve 1. The refrigerant liquid discharged from the high-temperature condenser 10 is depressurized and cooled, and then enters the steam generator 13 to absorb heat, heat up, and vaporize. The refrigerant steam discharged from the steam generator 13 is provided to the ejector 14 as working steam. The working steam enters the ejector 14, flows through the nozzle to depressurize and increase speed, and forms a low pressure. The refrigerant steam generated by the evaporator 9 is drawn into the low-pressure zone of the ejector 14. After the two steams are mixed, they flow through the diffuser to depressurize and increase pressure to form medium-pressure steam and are supplied to the absorber 6. The high-temperature heat medium provides high-temperature driving heat load through the high-temperature generator 5 and the steam generator 13. The heated medium obtains medium-temperature heating load through the absorber 6 and the high-temperature condenser 10. The low-temperature heat medium provides low-temperature heat load through the evaporator 9. The cooling medium carries away the low-temperature discharge heat load through the low-temperature condenser 7, forming the fourth type of ejector-absorption heat pump.
[0032] Figure 2 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0033] (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 high-temperature condenser, a throttling valve, 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; and the high-temperature generator 5 also has a refrigerant vapor channel... The high-temperature condenser 10 is connected to the high-temperature condenser 10. The high-temperature condenser 10 is also connected to the low-temperature generator 1 via a refrigerant liquid pipeline. The low-temperature generator 1 is then connected to the evaporator 9 via a refrigerant liquid pipeline through a throttle valve 11. The high-temperature condenser 10 is also connected to the outside via a refrigerant liquid pipeline. The outside has a working steam channel connected to the high-pressure steam inlet of the ejector 14. The evaporator 9 also has a refrigerant steam channel connected to the low-pressure steam inlet of the ejector 14. The ejector 14 also has a medium-pressure refrigerant steam channel connected to the absorber 6. The high-temperature generator 5 is also connected to the outside via a high-temperature heat medium channel. The absorber 6 and the high-temperature condenser 10 are also connected to the outside via heated medium channels. The low-temperature condenser 7 is also connected to the outside via a cooling medium channel. The evaporator 9 is also connected to the outside via a low-temperature heat medium channel.
[0034] (2) In terms of process, with Figure 1 Compared to the fourth type of jet-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 10 is divided into two paths - the first path is provided to the low-temperature generator 1 as the driving heat medium and the second path is discharged to the outside, and the outside provides working steam to the ejector 14, thus forming the fourth type of jet-absorption heat pump.
[0035] Figure 3 The fourth type of jet-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 high-temperature condenser, a throttling valve, 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 high-temperature condenser 10. The high-temperature condenser 10 also has a refrigerant liquid line connected to the low-temperature generator 1. After that, the low-temperature generator 1 has a refrigerant liquid line connected to the evaporator 9 via the throttle valve 11. The high-temperature generator 5 also has a refrigerant vapor channel connected to the high-pressure steam inlet of the ejector 14. The evaporator 9 also has a refrigerant vapor channel connected to the low-pressure steam inlet of the ejector 14. The ejector 14 also has a medium-pressure refrigerant vapor channel connected to the absorber 6. The high-temperature generator 5 also has a high-temperature heat medium channel connected to the outside. The absorber 6 and the high-temperature condenser 10 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 evaporator 9 also has a low-temperature heat medium channel connected to the outside.
[0037] (2) In terms of process, with Figure 1 Compared to the fourth type of jet-absorption heat pump shown, the difference is that the refrigerant liquid in the high-temperature condenser 10 is entirely supplied to the low-temperature generator 1 as the driving heat medium, and the refrigerant vapor released by the high-temperature generator 5 is divided into two paths - the first path enters the high-temperature condenser 10 to release heat and condense, and the second path is supplied to the ejector 14 as working steam, thus forming the fourth type of jet-absorption heat pump.
[0038] Figure 4 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0039] (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 high-temperature condenser, a throttle valve, a high-pressure pump, a steam generator, an ejector, and a second solution pump; the absorber 6 has a dilute solution pipeline connected to the high-temperature generator 5 via the solution pump 2 and the solution heat exchanger 3; the high-temperature generator 5 also has a concentrated solution pipeline connected to the low-temperature generator 1 via the solution heat exchanger 3 and the second solution heat exchanger 4; the low-temperature generator 1 also has a concentrated solution pipeline connected to the absorber 6 via the second solution pump 15 and the second solution heat exchanger 4; 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; and the high-temperature generator 5 also has a refrigerant vapor channel. The high-temperature condenser 10 is connected to the high-temperature condenser 10. The high-temperature condenser 10 is also connected to the low-temperature generator 1 via a refrigerant liquid pipeline. The low-temperature generator 1 is then connected to the evaporator 9 via a refrigerant liquid pipeline through a throttle valve 11. The high-temperature condenser 10 is also connected to the steam generator 13 via a high-pressure pump 12. The steam generator 13 is also connected to the high-pressure steam inlet of the ejector 14 via a refrigerant steam channel. The evaporator 9 is also connected to the low-pressure steam inlet of the ejector 14 via a refrigerant steam channel. The ejector 14 is also connected to the absorber 6 via a medium-pressure refrigerant steam channel. The high-temperature generator 5 and the steam generator 13 are also connected to the outside via high-temperature heat medium channels. The absorber 6 and the high-temperature condenser 10 are also connected to the outside via heated medium channels. The low-temperature condenser 7 is also connected to the outside via a cooling medium channel. The evaporator 9 is also connected to the outside via a low-temperature heat medium channel.
[0040] (2) In terms of process, the dilute solution from 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, heating the solution inside and releasing refrigerant vapor, which is then supplied to high-temperature condenser 10. The concentrated solution from high-temperature generator 5 enters low-temperature generator 1 via solution heat exchanger 3 and second solution heat exchanger 4, absorbing heat and releasing refrigerant vapor, which is then supplied to low-temperature condenser 7. The concentrated solution from low-temperature generator 1 enters absorber 6 via second solution pump 15 and second solution heat exchanger 4, absorbing refrigerant vapor and releasing heat to the heated medium. The refrigerant vapor from low-temperature condenser 7 releases heat to the cooling medium to form refrigerant liquid. The refrigerant liquid from low-temperature condenser 7 is pressurized by low-pressure pump 8 and enters evaporator 9 to absorb heat and vaporize. The refrigerant vapor from high-temperature condenser 10 releases heat to the heated medium to form refrigerant liquid. The first path of refrigerant liquid discharged from high-temperature condenser 10 flows through generator 1 to release heat and cool down, and then flows through... Throttling valve 11 reduces pressure and temperature, then enters evaporator 9 to absorb heat and vaporize. The second stream of refrigerant liquid discharged from high-temperature condenser 10 flows through high-pressure pump 12 to increase pressure and enters steam generator 13 to absorb heat, increase temperature, and vaporize. The refrigerant steam discharged from steam generator 13 is provided to ejector 14 as working steam. The working steam enters ejector 14, flows through nozzles to reduce pressure and increase speed, and forms low pressure. The refrigerant steam generated by evaporator 9 is drawn into the low-pressure zone of ejector 14. After the two streams of steam are mixed, they flow through diffuser to reduce speed and increase pressure, forming medium-pressure steam, which is then supplied to absorber 6. High-temperature heat medium provides high-temperature driving heat load through high-temperature generator 5 and steam generator 13. The heated medium obtains medium-temperature heating load through absorber 6 and high-temperature condenser 10. Low-temperature heat medium provides low-temperature heat load through evaporator 9. Cooling medium carries away low-temperature discharge heat load through low-temperature condenser 7, forming the fourth type of jet-absorption heat pump.
[0041] Figure 5 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0042] (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 high-temperature condenser, a throttle valve, an ejector, and a second solution pump; the absorber 6 has a dilute solution pipeline connected to the high-temperature generator 5 via the solution pump 2 and the solution heat exchanger 3; the high-temperature generator 5 also has a concentrated solution pipeline connected to the low-temperature generator 1 via the solution heat exchanger 3 and the second solution heat exchanger 4; the low-temperature generator 1 also has a concentrated solution pipeline connected to the absorber 6 via the second solution pump 15 and the second solution heat exchanger 4; 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... There is also a refrigerant vapor channel connected to the high-temperature condenser 10. The high-temperature condenser 10 also has a refrigerant liquid line connected to the low-temperature generator 1. After that, the low-temperature generator 1 has a refrigerant liquid line connected to the evaporator 9 via the throttle valve 11. The high-temperature condenser 10 also has a refrigerant liquid line connected to the outside. The outside has a working steam channel connected to the high-pressure steam inlet of the ejector 14. The evaporator 9 also has a refrigerant vapor channel connected to the low-pressure steam inlet of the ejector 14. The ejector 14 also has a medium-pressure refrigerant vapor channel connected to the absorber 6. The high-temperature generator 5 also has a high-temperature heat medium channel connected to the outside. The absorber 6 and the high-temperature condenser 10 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 evaporator 9 also has a low-temperature heat medium channel connected to the outside.
[0043] (2) In terms of process, with Figure 4 Compared to the fourth type of jet-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 10 is divided into two paths - the first path is provided to the low-temperature generator 1 as the driving heat medium and the second path is discharged to the outside, and the outside provides working steam to the ejector 14, thus forming the fourth type of jet-absorption heat pump.
[0044] Figure 6 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0045] (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 high-temperature condenser, a throttle valve, an ejector, and a second solution pump; the absorber 6 has a dilute solution pipeline connected to the high-temperature generator 5 via the solution pump 2 and the solution heat exchanger 3; the high-temperature generator 5 also has a concentrated solution pipeline connected to the low-temperature generator 1 via the solution heat exchanger 3 and the second solution heat exchanger 4; the low-temperature generator 1 also has a concentrated solution pipeline connected to the absorber 6 via the second solution pump 15 and the second solution heat exchanger 4; the low-temperature generator 1 also has a refrigerant vapor channel connected to the low-temperature condenser 7; and 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 is connected to the high-temperature condenser 10 via a refrigerant vapor channel. The high-temperature condenser 10 is connected to the low-temperature generator 1 via a refrigerant liquid line. The low-temperature generator 1 is then connected to the evaporator 9 via a refrigerant liquid line through a throttle valve 11. The high-temperature generator 5 is also connected to the high-pressure steam inlet of the ejector 14 via a refrigerant vapor channel. The evaporator 9 is also connected to the low-pressure steam inlet of the ejector 14 via a refrigerant vapor channel. The ejector 14 is also connected to the absorber 6 via a medium-pressure refrigerant vapor channel. The high-temperature generator 5 is also connected to the outside via a high-temperature heat medium channel. The absorber 6 and the high-temperature condenser 10 are also connected to the outside via heated medium channels. The low-temperature condenser 7 is also connected to the outside via a cooling medium channel. The evaporator 9 is also connected to the outside via a low-temperature heat medium channel.
[0046] (2) In terms of process, with Figure 4 Compared to the fourth type of jet-absorption heat pump shown, the difference is that the refrigerant liquid in the high-temperature condenser 10 is entirely supplied to the low-temperature generator 1 as the driving heat medium, and the refrigerant vapor released by the high-temperature generator 5 is divided into two paths—the first path enters the high-temperature condenser 10 to release heat and condense, and the second path is supplied to the ejector 14 as working steam, thus forming the fourth type of jet-absorption heat pump.
[0047] Figure 7 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0048] (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, an evaporator, a high-temperature condenser, a throttling valve, a high-pressure pump, a steam generator, an ejector, a second solution pump, and a second absorber; the absorber 6 has a dilute solution pipeline connected to the second absorber 16 via the solution heat exchanger 3, the second absorber 16 also has a dilute solution pipeline connected to the high-temperature generator 5 via the solution pump 2 and the second solution heat exchanger 4, the high-temperature generator 5 also has a concentrated solution pipeline connected to the low-temperature generator 1 via the second solution heat exchanger 4, the low-temperature generator 1 also has a concentrated solution pipeline connected to the absorber 6 via the second solution pump 15 and the solution heat exchanger 3, the low-temperature generator 1 also has a refrigerant vapor channel connected to the second absorber 16, and the high-temperature generator 5 also has a refrigerant vapor channel connected to the high-temperature condenser. Condenser 10 is connected, and the high-temperature condenser 10 is also connected to the low-temperature generator 1 via a refrigerant liquid pipeline. The low-temperature generator 1 is then connected to the evaporator 9 via a refrigerant liquid pipeline through a throttle valve 11. The high-temperature condenser 10 is also connected to the steam generator 13 via a refrigerant liquid pipeline through a high-pressure pump 12. The steam generator 13 is also connected to the high-pressure steam inlet of the ejector 14 via a refrigerant steam channel. The evaporator 9 is also connected to the low-pressure steam inlet of the ejector 14 via a refrigerant steam channel. The ejector 14 is also connected to the absorber 6 via a medium-pressure refrigerant steam channel. The high-temperature generator 5 and the steam generator 13 are also connected to the outside via high-temperature heat medium channels. The absorber 6 and the high-temperature condenser 10 are also connected to the outside via heated medium channels. The evaporator 9 is also connected to the outside via a low-temperature heat medium channel. The second absorber 16 is also connected to the outside via a cooling medium channel.
[0049] (2) In terms of process, the dilute solution of absorber 6 enters the second absorber 16 through solution heat exchanger 3, absorbs refrigerant vapor and releases heat to the cooling medium. The dilute solution of the second absorber 16 enters the high-temperature generator 5 through 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 supplies it to the high-temperature condenser 10. The concentrated solution of the high-temperature generator 5 enters the low-temperature generator 1 through the second solution heat exchanger 4, absorbs heat and releases refrigerant vapor and supplies it to the second absorber 16. The concentrated solution of the low-temperature generator 1 enters the absorber 6 through the second solution pump 15 and solution heat exchanger 3, absorbs refrigerant vapor and releases heat to the heated medium. The refrigerant vapor of the high-temperature condenser 10 releases heat to the heated medium to form refrigerant liquid. The first refrigerant liquid discharged from the high-temperature condenser 10 flows through the generator 1 to release heat and cool down, and flows through the throttle valve 11 to reduce pressure. The refrigerant liquid, cooled and vaporized in the evaporator 9, enters the steam generator 13 after being pressurized by the high-pressure pump 12 and then vaporized. The refrigerant steam discharged from the steam generator 13 is supplied to the ejector 14 as working steam. The working steam enters the ejector 14, flows through the nozzle to reduce pressure and increase speed, and forms a low pressure. The refrigerant steam generated by the evaporator 9 is drawn into the low-pressure zone of the ejector 14. After the two steam streams are mixed, 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 provides a high-temperature driving heat load through the high-temperature generator 5 and the steam generator 13. The heated medium obtains a medium-temperature heating load through the absorber 6 and the high-temperature condenser 10. The low-temperature heat medium provides a low-temperature heat load through the evaporator 9. The cooling medium carries away the low-temperature discharge heat load through the second absorber 16, forming a fourth type of jet-absorption heat pump.
[0050] Figure 8 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0051] (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, an evaporator, a high-temperature condenser, a throttle valve, an ejector, a second solution pump, and a second absorber; the absorber 6 has a dilute solution pipeline connected to the second absorber 16 via the solution heat exchanger 3, the second absorber 16 also has a dilute solution pipeline connected to the high-temperature generator 5 via the solution pump 2 and the second solution heat exchanger 4, the high-temperature generator 5 also has a concentrated solution pipeline connected to the low-temperature generator 1 via the second solution heat exchanger 4, the low-temperature generator 1 also has a concentrated solution pipeline connected to the absorber 6 via the second solution pump 15 and the solution heat exchanger 3, the low-temperature generator 1 also has a refrigerant vapor channel connected to the second absorber 16, and the high-temperature generator 5 also has The refrigerant vapor passage is connected to the high-temperature condenser 10. The high-temperature condenser 10 also has a refrigerant liquid pipeline connected to the low-temperature generator 1. The low-temperature generator 1 then has a refrigerant liquid pipeline connected to the evaporator 9 via the throttle valve 11. The high-temperature condenser 10 also has a refrigerant liquid pipeline connected to the outside. The outside has a working steam passage connected to the high-pressure steam inlet of the ejector 14. The evaporator 9 also has a refrigerant vapor passage connected to the low-pressure steam inlet of the ejector 14. The ejector 14 also has a medium-pressure refrigerant vapor passage connected to the absorber 6. The high-temperature generator 5 also has a high-temperature heat medium passage connected to the outside. The absorber 6 and the high-temperature condenser 10 also have heated medium passages connected to the outside. The evaporator 9 also has a low-temperature heat medium passage connected to the outside. The second absorber 16 also has a cooling medium passage connected to the outside.
[0052] (2) In terms of process, with Figure 7 Compared to the fourth type of jet-absorption heat pump shown, the difference is that the refrigerant liquid discharged from the high-temperature condenser 10 is divided into two paths - the first path is provided to the low-temperature generator 1 as the driving heat medium and the second path is discharged to the outside, and the outside provides working steam to the ejector 14, thus forming the fourth type of jet-absorption heat pump.
[0053] Figure 9 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0054] (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, an evaporator, a high-temperature condenser, a throttling valve, an ejector, a second solution pump, and a second absorber; the absorber 6 has a dilute solution pipeline connected to the second absorber 16 via the solution heat exchanger 3, the second absorber 16 also has a dilute solution pipeline connected to the high-temperature generator 5 via the solution pump 2 and the second solution heat exchanger 4, the high-temperature generator 5 also has a concentrated solution pipeline connected to the low-temperature generator 1 via the second solution heat exchanger 4, the low-temperature generator 1 also has a concentrated solution pipeline connected to the absorber 6 via the second solution pump 15 and the solution heat exchanger 3, the low-temperature generator 1 also has a refrigerant vapor channel connected to the second absorber 16, and the high-temperature condenser... The high-temperature generator 5 is connected to the high-temperature condenser 10 via a refrigerant vapor channel. The high-temperature condenser 10 is connected to the low-temperature generator 1 via a refrigerant liquid line. The low-temperature generator 1 is then connected to the evaporator 9 via a refrigerant liquid line through a throttle valve 11. The high-temperature generator 5 is also connected to the high-pressure steam inlet of the ejector 14 via a refrigerant vapor channel. The evaporator 9 is also connected to the low-pressure steam inlet of the ejector 14 via a refrigerant vapor channel. The ejector 14 is also connected to the absorber 6 via a medium-pressure refrigerant vapor channel. The high-temperature generator 5 is also connected to the outside via a high-temperature heat medium channel. The absorber 6 and the high-temperature condenser 10 are also connected to the outside via heated medium channels. The evaporator 9 is also connected to the outside via a low-temperature heat medium channel. The second absorber 16 is also connected to the outside via a cooling medium channel.
[0055] (2) In terms of process, with Figure 7 Compared to the fourth type of jet-absorption heat pump shown, the difference is that the refrigerant liquid in the high-temperature condenser 10 is entirely supplied to the low-temperature generator 1 as the driving heat medium, and the refrigerant vapor released by the high-temperature generator 5 is divided into two paths - the first path enters the high-temperature condenser 10 to release heat and condense, and the second path is supplied to the ejector 14 as working steam, thus forming the fourth type of jet-absorption heat pump.
[0056] Figure 10 The fourth type of jet-absorption heat pump shown is implemented as follows:
[0057] exist Figure 7 In the fourth type of jet-absorption heat pump shown, a nozzle A is added and replaces the throttle valve 11; the refrigerant liquid discharged from the high-temperature condenser 10 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, and the second path is pressurized by the high-pressure pump 12 and then enters the steam generator 13 to absorb heat and vaporize, thus forming the fourth type of jet-absorption heat pump.
[0058] The effects achievable by this invention—the fourth type of jet-absorption heat pump proposed in this invention has the following effects and advantages:
[0059] (1) A new technology for thermal energy-driven refrigeration / heating was proposed, which enriched the thermal energy refrigeration / heating technology.
[0060] (2) Effectively improve the working parameters of refrigerant vapor, significantly expand the working parameter range of heat pump, and facilitate the realization of cooling and heating over a larger temperature range.
[0061] (3) The process is reasonable and the performance index is reasonable.
[0062] (4) Simple structure, reducing manufacturing costs.
[0063] (5) It is conducive to the full utilization of high-grade thermal energy and reduces the irreversible loss of systemic temperature difference.
[0064] (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.
[0065] (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.
[0066] (8) It provides a variety of specific technical solutions, which can cope with many different actual situations and has a wide range of applications, which is conducive to expanding the application scope and value of jet-absorption heat pump technology.
Claims
1. The fourth type of jet-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 high-temperature condenser, a throttling 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 high-temperature condenser (10); the high-temperature... After the condenser (10) is connected to the low-temperature generator (1) via a refrigerant liquid pipeline, the low-temperature generator (1) is connected to the evaporator (9) via a refrigerant liquid pipeline through a throttle valve (11). The high-temperature condenser (10) is connected to the steam generator (13) via a refrigerant liquid pipeline through a high-pressure pump (12). The steam generator (13) is connected to the high-pressure steam inlet of the ejector (14) via a refrigerant steam channel. The evaporator (9) is connected to the low-pressure steam inlet of the ejector (14) via a refrigerant steam channel. The ejector (14) is connected to the absorber (6) via a medium-pressure refrigerant steam channel. The high-temperature generator (5) and the steam generator (13) are connected to the outside via high-temperature heat medium channels. The absorber (6) and the high-temperature condenser (10) are connected to the outside via heated medium channels. The low-temperature condenser (7) is connected to the outside via a cooling medium channel. The evaporator (9) is connected to the outside via a low-temperature heat medium channel, forming a fourth type of jet-absorption heat pump.
2. The fourth type of jet-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 high-temperature condenser, a throttling valve, 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 high-temperature condenser (9). The condenser (10) is connected, and the high-temperature condenser (10) is also connected to the low-temperature generator (1) via a refrigerant liquid pipeline. The low-temperature generator (1) is then connected to the evaporator (9) via a refrigerant liquid pipeline through a throttle valve (11). The high-temperature condenser (10) is also connected to the outside via a refrigerant liquid pipeline. The outside has a working steam channel connected to the high-pressure steam inlet of the ejector (14). The evaporator (9) also has a refrigerant steam channel connected to the low-pressure steam inlet of the ejector (14). The ejector (14) also has a medium-pressure refrigerant steam channel connected to the absorber (6). The high-temperature generator (5) also has a high-temperature heat medium channel connected to the outside. The absorber (6) and the high-temperature condenser (10) 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 evaporator (9) also has a low-temperature heat medium channel connected to the outside, forming a fourth type of jet-absorption heat pump.
3. The fourth type of jet-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 high-temperature condenser, a throttling valve, 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 evaporator (9). The refrigerant vapor channel is connected to the high-temperature condenser (10). The high-temperature condenser (10) also has a refrigerant liquid pipeline connected to the low-temperature generator (1). The low-temperature generator (1) then has a refrigerant liquid pipeline connected to the evaporator (9) via the throttle valve (11). The high-temperature generator (5) also has a refrigerant vapor channel connected to the high-pressure steam inlet of the ejector (14). The evaporator (9) also has a refrigerant vapor channel connected to the low-pressure steam inlet of the ejector (14). The ejector (14) also has a medium-pressure refrigerant vapor channel connected to the absorber (6). The high-temperature generator (5) also has a high-temperature heat medium channel connected to the outside. The absorber (6) and the high-temperature condenser (10) 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 evaporator (9) also has a low-temperature heat medium channel connected to the outside, forming a fourth type of jet-absorption heat pump.
4. The fourth type of jet-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 high-temperature condenser, a throttling valve, a high-pressure pump, a steam generator, an ejector, and a second solution pump; the absorber (6) has a dilute solution pipeline connected to the high-temperature generator (5) via the solution pump (2) and the solution heat exchanger (3); the high-temperature generator (5) also has a concentrated solution pipeline connected to the low-temperature generator (1) via the solution heat exchanger (3) and the second solution heat exchanger (4); the low-temperature generator (1) also has a concentrated solution pipeline connected to the absorber (6) via the second solution pump (15) and the second solution heat exchanger (4); 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 high-temperature condenser (9). 10) Connected, the high temperature condenser (10) and the refrigerant liquid pipeline are connected to the low temperature generator (1). The low temperature generator (1) is then connected to the evaporator (9) via the throttle valve (11). The high temperature condenser (10) and the refrigerant liquid pipeline are connected to the steam generator (13) via the high pressure pump (12). The steam generator (13) and the refrigerant steam channel are connected to the high pressure steam inlet of the ejector (14). The evaporator (9) and the refrigerant steam channel are connected to the low pressure steam inlet of the ejector (14). The ejector (14) and the medium pressure refrigerant steam channel are connected to the absorber (6). The high temperature generator (5) and the steam generator (13) are also connected to the outside via high temperature heat medium channels. The absorber (6) and the high temperature condenser (10) are also connected to the outside via heated medium channels. The low temperature condenser (7) and the low temperature condenser (9) are also connected to the outside via cooling medium channels. The evaporator (9) and the low temperature heat medium channels are connected to the outside, forming a fourth type of jet-absorption heat pump.
5. The fourth type of jet-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 high-temperature condenser, a throttle valve, an ejector, and a second solution pump; the absorber (6) has a dilute solution pipeline connected to the high-temperature generator (5) via the solution pump (2) and the solution heat exchanger (3); the high-temperature generator (5) also has a concentrated solution pipeline connected to the low-temperature generator (1) via the solution heat exchanger (3) and the second solution heat exchanger (4); the low-temperature generator (1) also has a concentrated solution pipeline connected to the absorber (6) via the second solution pump (15) and the second solution heat exchanger (4); 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 evaporator (9). The refrigerant vapor channel is connected to the high-temperature condenser (10). The high-temperature condenser (10) also has a refrigerant liquid pipeline connected to the low-temperature generator (1). The low-temperature generator (1) then has a refrigerant liquid pipeline connected to the evaporator (9) via a throttle valve (11). The high-temperature condenser (10) also has a refrigerant liquid pipeline connected to the outside. The outside has a working steam channel connected to the high-pressure steam inlet of the ejector (14). The evaporator (9) also has a refrigerant vapor channel connected to the low-pressure steam inlet of the ejector (14). The ejector (14) also has a medium-pressure refrigerant vapor channel connected to the absorber (6). The high-temperature generator (5) also has a high-temperature heat medium channel connected to the outside. The absorber (6) and the high-temperature condenser (10) 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 evaporator (9) also has a low-temperature heat medium channel connected to the outside, forming a fourth type of jet-absorption heat pump.
6. The fourth type of jet-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 high-temperature condenser, a throttle valve, an ejector, and a second solution pump; the absorber (6) has a dilute solution pipeline connected to the high-temperature generator (5) via the solution pump (2) and the solution heat exchanger (3); the high-temperature generator (5) also has a concentrated solution pipeline connected to the low-temperature generator (1) via the solution heat exchanger (3) and the second solution heat exchanger (4); the low-temperature generator (1) also has a concentrated solution pipeline connected to the absorber (6) via the second solution pump (15) and the second solution heat exchanger (4); 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... The generator (5) is connected to the high-temperature condenser (10) via a refrigerant vapor channel. The high-temperature condenser (10) is connected to the low-temperature generator (1) via a refrigerant liquid pipeline. The low-temperature generator (1) is then connected to the evaporator (9) via a refrigerant liquid pipeline through a throttle valve (11). The high-temperature generator (5) is connected to the high-pressure steam inlet of the ejector (14) via a refrigerant vapor channel. The evaporator (9) is connected to the low-pressure steam inlet of the ejector (14) via a refrigerant vapor channel. The ejector (14) is connected to the absorber (6) via a medium-pressure refrigerant vapor channel. The high-temperature generator (5) is connected to the outside via a high-temperature heat medium channel. The absorber (6) and the high-temperature condenser (10) are connected to the outside via heated medium channels. The low-temperature condenser (7) is connected to the outside via a cooling medium channel. The evaporator (9) is connected to the outside via a low-temperature heat medium channel, forming a fourth type of jet-absorption heat pump.
7. The fourth type of jet-absorption heat pump is mainly composed of a low-temperature generator, a solution pump, a solution heat exchanger, a second solution heat exchanger, a high-temperature generator, an absorber, an evaporator, a high-temperature condenser, a throttling valve, a high-pressure pump, a steam generator, an ejector, a second solution pump, and a second absorber. The absorber (6) has a dilute solution pipeline connected to the second absorber (16) via the solution heat exchanger (3). The second absorber (16) also has a dilute solution pipeline connected to the high-temperature generator (5) via the solution pump (2) and the second solution heat exchanger (4). The high-temperature generator (5) also has a concentrated solution pipeline connected to the low-temperature generator (1) via the second solution heat exchanger (4). The low-temperature generator (1) also has a concentrated solution pipeline connected to the absorber (6) via the second solution pump (15) and the solution heat exchanger (3). The low-temperature generator (1) also has a refrigerant vapor channel connected to the second absorber (16). The high-temperature generator (5) also has a refrigerant vapor channel connected to the high-temperature condenser (10). After the high-temperature condenser (10) is connected to the low-temperature generator (1), the low-temperature generator (1) is connected to the evaporator (9) via the throttle valve (11). The high-temperature condenser (10) is connected to the steam generator (13) via the high-pressure pump (12). The steam generator (13) is connected to the high-pressure steam inlet of the ejector (14) via the refrigerant steam channel. The evaporator (9) is connected to the low-pressure steam inlet of the ejector (14) via the refrigerant steam channel. The ejector (14) is connected to the absorber (6) via the medium-pressure refrigerant steam channel. The high-temperature generator (5) and the steam generator (13) are connected to the outside via high-temperature heat medium channels. The absorber (6) and the high-temperature condenser (10) are connected to the outside via heated medium channels. The evaporator (9) is connected to the outside via low-temperature heat medium channels. The second absorber (16) is connected to the outside via cooling medium channels, forming a fourth type of jet-absorption heat pump.
8. The fourth type of jet-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, an evaporator, a high-temperature condenser, a throttling valve, an ejector, a second solution pump, and a second absorber; the absorber (6) has a dilute solution pipeline connected to the second absorber (16) via the solution heat exchanger (3), the second absorber (16) also has a dilute solution pipeline connected to the high-temperature generator (5) via the solution pump (2) and the second solution heat exchanger (4), the high-temperature generator (5) also has a concentrated solution pipeline connected to the low-temperature generator (1) via the second solution heat exchanger (4), the low-temperature generator (1) also has a concentrated solution pipeline connected to the absorber (6) via the second solution pump (15) and the solution heat exchanger (3), the low-temperature generator (1) also has a refrigerant vapor channel connected to the second absorber (16), and the high-temperature generator (5) also has refrigerant vapor... The channel is connected to the high-temperature condenser (10). The high-temperature condenser (10) also has a refrigerant liquid pipeline connected to the low-temperature generator (1). The low-temperature generator (1) then has a refrigerant liquid pipeline connected to the evaporator (9) via the throttle valve (11). The high-temperature condenser (10) also has a refrigerant liquid pipeline connected to the outside. The outside has a working steam channel connected to the high-pressure steam inlet of the ejector (14). The evaporator (9) also has a refrigerant steam channel connected to the low-pressure steam inlet of the ejector (14). The ejector (14) also has a medium-pressure refrigerant steam channel connected to the absorber (6). The high-temperature generator (5) also has a high-temperature heat medium channel connected to the outside. The absorber (6) and the high-temperature condenser (10) also have heated medium channels connected to the outside. The evaporator (9) also has a low-temperature heat medium channel connected to the outside. The second absorber (16) also has a cooling medium channel connected to the outside, forming a fourth type of jet-absorption heat pump.
9. The fourth type of jet-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, an evaporator, a high-temperature condenser, a throttling valve, an ejector, a second solution pump, and a second absorber; the absorber (6) has a dilute solution pipeline connected to the second absorber (16) via the solution heat exchanger (3), the second absorber (16) also has a dilute solution pipeline connected to the high-temperature generator (5) via the solution pump (2) and the second solution heat exchanger (4), the high-temperature generator (5) also has a concentrated solution pipeline connected to the low-temperature generator (1) via the second solution heat exchanger (4), the low-temperature generator (1) also has a concentrated solution pipeline connected to the absorber (6) via the second solution pump (15) and the solution heat exchanger (3), the low-temperature generator (1) also has a refrigerant vapor channel connected to the second absorber (16), the high-temperature generator (5) There is also a refrigerant vapor channel connected to the high-temperature condenser (10), and the high-temperature condenser (10) is also connected to the low-temperature generator (1) via a refrigerant liquid pipeline. The low-temperature generator (1) is then connected to the evaporator (9) via a refrigerant liquid pipeline through a throttle valve (11). The high-temperature generator (5) is also connected to the high-pressure steam inlet of the ejector (14) via a refrigerant vapor channel. The evaporator (9) is also connected to the low-pressure steam inlet of the ejector (14) via a refrigerant vapor channel. The ejector (14) is also connected to the absorber (6) via a medium-pressure refrigerant vapor channel. The high-temperature generator (5) is also connected to the outside via a high-temperature heat medium channel. The absorber (6) and the high-temperature condenser (10) are also connected to the outside via heated medium channels. The evaporator (9) is also connected to the outside via a low-temperature heat medium channel. The second absorber (16) is also connected to the outside via a cooling medium channel, forming a fourth type of jet-absorption heat pump.
10. A fourth type of jet-absorption heat pump is formed by adding a nozzle (A) and replacing the throttle valve (11) in any of the fourth type of jet-absorption heat pumps described in claims 1-9.