CN106225302B - First-class thermally driven compression-absorption heat pump - Google Patents
First-class thermally driven compression-absorption heat pump Download PDFInfo
- Publication number
- CN106225302B CN106225302B CN201610522622.XA CN201610522622A CN106225302B CN 106225302 B CN106225302 B CN 106225302B CN 201610522622 A CN201610522622 A CN 201610522622A CN 106225302 B CN106225302 B CN 106225302B
- Authority
- CN
- China
- Prior art keywords
- generator
- communicated
- solution
- heat
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/02—Compression-sorption machines, plants, or systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
- F25B41/30—Expansion means; Dispositions thereof
Abstract
The invention provides a first type of thermally driven compression-absorption heat pump, and belongs to the technical field of power, refrigeration and heat pumps. The absorber, the generator, the solution pump and the solution heat exchanger form a solution circulating system, the generator is provided with a refrigerant steam channel communicated with the compressor, the compressor is provided with a refrigerant steam channel communicated with the condenser, the condenser is communicated with the evaporator through a throttle valve, the condenser is communicated with the high-temperature heat exchanger through a refrigerant liquid pump, the high-temperature heat exchanger is provided with a refrigerant steam channel communicated with the expander, the expander is provided with a refrigerant steam channel communicated with the second condenser, the second condenser is communicated with the evaporator through a second refrigerant liquid pump, the evaporator is provided with a refrigerant steam channel communicated with the absorber, the generator and the high-temperature heat exchanger are provided with, the absorber and the condenser are provided with heated medium channels, the evaporator is provided with a low-temperature heat medium channel, the second condenser is provided with a cooling medium channel which is respectively communicated with the outside, and the expander is connected with the compressor and transmits power to form a first type of heat-driven compression-absorption heat pump.
Description
The technical field is as follows:
The invention belongs to the technical field of power, refrigeration and heat pumps.
Background art:
Cold demand, heat demand and power demand, which are common in human life and production; in reality, people often need to use high-temperature heat energy to realize refrigeration, heat supply or power conversion, and also need to use power to refrigerate or use power and combine low-temperature heat energy to supply heat. In the process of achieving the above purpose, various conditions are faced, such as the type, grade and quantity of energy, the type, grade and quantity of user requirements, the type of working medium, the flow, structure and manufacturing cost of equipment, the safety of equipment operation, the acceptable degree of environmental temperature and environment, and the like.
A heat energy (temperature difference) utilization technology represented by an absorption heat pump technology, and high-temperature heat load driving is utilized to realize heat supply or refrigeration; due to the influence of the properties of the working medium (solution and refrigerant medium), a high-temperature heat load with an excessively high temperature or a low-temperature heat load with an excessively low temperature cannot be reasonably applied to the flow of the absorption heat pump, so that the application field and the application range of the absorption heat pump are greatly limited. Compression heat pump technology has better flexibility in thermodynamic performance, but the core component of the compression heat pump is a moving component, which brings many disadvantages-for example, noise generated in the operation of the compression heat pump is intolerable; for this reason, it is considered to reduce the use and number of large moving parts (mainly compressors and expanders).
In order to exert the technical advantages of the absorption heat pump and give consideration to the requirements of power drive or external power supply, the invention provides a temperature difference utilization link consisting of a refrigerant liquid pump, a high-temperature heat exchanger, an expander, a compressor, a second condenser and a second refrigerant liquid pump, which is used for effectively utilizing the temperature difference between a high-temperature heat source and a heated medium or the temperature difference between the high-temperature heat source and the environment and has comprehensive advantages.
The invention content is as follows:
The invention mainly aims to provide a series of first-class thermally driven compression-absorption heat pumps, and the specific contents of the invention are explained in different terms as follows:
1. The first kind of heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a compressor, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a refrigerant liquid pump, a high-temperature heat exchanger, an expansion machine, a second condenser and a second refrigerant liquid pump; the absorber is provided with a dilute solution pipeline communicated with the generator through a solution pump and a solution heat exchanger, the generator is also provided with a concentrated solution pipeline communicated with the absorber through the solution heat exchanger, the generator is also provided with a refrigerant steam channel communicated with the compressor, the compressor is also provided with a refrigerant steam channel communicated with the condenser, the condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through a throttle valve, the condenser is also provided with a refrigerant liquid pipeline communicated with the high temperature heat exchanger through a refrigerant liquid pump, then the high temperature heat exchanger is further provided with a refrigerant steam channel communicated with the expander, the expander is also provided with a refrigerant steam channel communicated with a second condenser, the second condenser is also provided with a refrigerant liquid pipeline communicated with the evaporator through a second refrigerant liquid pump, the evaporator is also provided with a refrigerant steam channel communicated with the absorber, the generator and the high temperature heat exchanger are also respectively provided with a high temperature heat medium channel communicated with, the evaporator is also provided with a low-temperature heat medium channel communicated with the outside, the second condenser is also provided with a cooling medium channel communicated with the outside, and the expander is connected with the compressor and transmits power to form a first type of heat-driven compression-absorption heat pump; wherein, or the expander is connected with the compressor, the refrigerant liquid pump, the second refrigerant liquid pump and the solution pump and transmits power.
2. A first type of heat-driven compression-absorption heat pump is characterized in that a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added in the first type of heat-driven compression-absorption heat pump in item 1, a dilute solution pipeline is additionally arranged on an absorber and is communicated with the second generator through the second solution pump and the second solution heat exchanger, a concentrated solution pipeline is also communicated with the absorber through the second solution heat exchanger, a refrigerant steam channel of the generator is communicated with a compressor, the refrigerant liquid pipeline of the second generator is communicated with a condenser through the second throttle valve after the generator is communicated with the second generator through the refrigerant steam channel, and the refrigerant steam channel of the second generator is communicated with the compressor to form the first type of heat-driven compression-absorption heat pump.
3. A first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second throttle valve and a second solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump described in item 1, a dilute solution pipeline of an absorber is communicated with the generator through the solution pump and the solution heat exchanger and is adjusted to be communicated with the generator through the dilute solution pipeline of the absorber through the solution pump, the solution heat exchanger and the second solution heat exchanger, a concentrated solution pipeline of the generator is communicated with the absorber through the solution heat exchanger and is adjusted to be communicated with the generator through a concentrated solution pipeline, the second generator is communicated with the second generator through the second solution heat exchanger, a concentrated solution pipeline of the second generator is communicated with the absorber through the solution heat exchanger, a refrigerant vapor channel of the generator is communicated with a compressor, and is adjusted to be communicated with the second generator through a refrigerant vapor channel, and then a refrigerant liquid pipeline of the second generator is communicated with a condenser through the second throttle valve, the second generator is also communicated with the compressor through a refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
4. a first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump described in item 1, a dilute solution pipeline of an absorber is communicated with the generator through the solution pump and the solution heat exchanger and is adjusted to be communicated with the second generator through the solution pump and the solution heat exchanger, a concentrated solution pipeline of the second generator is communicated with the generator through the second solution pump and the second solution heat exchanger, a concentrated solution pipeline of the generator is communicated with the absorber through the solution heat exchanger and is adjusted to be communicated with the generator through a concentrated solution pipeline of the generator through the second solution heat exchanger and the solution heat exchanger, a steam channel of the generator is adjusted to be communicated with a refrigerant steam channel of the compressor, and then a refrigerant liquid pipeline of the second generator is communicated with a condenser through the second throttle valve The second generator is also communicated with the compressor through a refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
5. a first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump described in item 1, the absorber is communicated with the generator through the solution pump and the solution heat exchanger and is adjusted to be communicated with the generator through the solution pump and the solution heat exchanger, the absorber is communicated with the second absorber through the solution pump and the solution heat exchanger, the second absorber is communicated with the generator through the second solution pump and the second solution heat exchanger through a dilute solution pipeline, the generator is communicated with the absorber through the solution heat exchanger and is adjusted to be communicated with the generator through a concentrated solution pipeline, the generator is communicated with the second generator through the second solution heat exchanger through a concentrated solution pipeline, the second generator is communicated with the absorber through the solution heat exchanger, and the second generator is also communicated with the second absorber through a refrigerant steam channel, the second generator is also provided with a high-temperature heat medium channel communicated with the outside, and the second absorber is also provided with a heated medium channel communicated with the outside to form a first type of heat-driven compression-absorption heat pump.
6. A first type of heat-driven compression-absorption heat pump is characterized in that a third generator, a second throttle valve, a third solution pump and a third solution heat exchanger are added in the first type of heat-driven compression-absorption heat pump in item 5, a dilute solution pipeline is additionally arranged on a second absorber and is communicated with the third generator through the third solution pump and the third solution heat exchanger, a concentrated solution pipeline is also communicated with the second generator through the third solution heat exchanger, a refrigerant steam channel of the generator is communicated with a compressor, the third generator is adjusted to be communicated with the third generator through the refrigerant steam channel, then the refrigerant liquid pipeline of the third generator is communicated with a condenser through the second throttle valve, and the refrigerant steam channel of the third generator is communicated with the compressor to form the first type of heat-driven compression-absorption heat pump.
7. a first heat-driven compression-absorption heat pump is characterized in that a third generator, a second throttle valve and a third solution heat exchanger are added in the first heat-driven compression-absorption heat pump described in the item 5, a dilute solution pipeline of a second absorber is communicated with a generator through a second solution pump and a second solution heat exchanger and is adjusted to be communicated with the generator through a second solution pump, a second solution heat exchanger and a third solution heat exchanger, a concentrated solution pipeline of the generator is communicated with the second generator through the second solution heat exchanger and is adjusted to be communicated with the generator through a concentrated solution pipeline, a concentrated solution pipeline of the third generator is communicated with the third generator through the third solution heat exchanger, a concentrated solution pipeline of the third generator is communicated with the second generator through the second solution heat exchanger, a refrigerant steam channel of the generator is communicated with a compressor and is adjusted to be communicated with the generator through a refrigerant steam channel of the generator and is communicated with the third generator, and then a refrigerant liquid pipeline of the third generator is communicated with the third generator through the second throttle valve The flow valve is communicated with the condenser, and the third generator is also communicated with the compressor through a refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
8. A first kind of heat-driven compression-absorption heat pump is characterized in that a third generator, a second throttle valve, a third solution pump and a third solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump described in item 5, a dilute solution pipeline of a second absorber is communicated with the generator through the second solution pump and the second solution heat exchanger and adjusted to be a dilute solution pipeline of the second absorber communicated with the third generator through the second solution pump and the second solution heat exchanger, a concentrated solution pipeline of the third generator is communicated with the generator through the third solution pump and the third solution heat exchanger, a concentrated solution pipeline of the generator is communicated with the second generator through the second solution heat exchanger and adjusted to be a concentrated solution pipeline of the generator communicated with the second generator through the third solution heat exchanger and the second solution heat exchanger, a refrigerant vapor channel of the generator is communicated with the compressor and adjusted to be a refrigerant vapor channel of the generator communicated with the third generator The third generator is also communicated with a compressor through a refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
9. The first kind of heat-driven compression-absorption heat pump is any one of the first kind of heat-driven compression-absorption heat pumps in items 2-4, a second throttle valve is omitted, a heat supply device is added, a second generator refrigerant liquid pipeline is communicated with a condenser through the second throttle valve and adjusted to be communicated with the condenser through the heat supply device, and the heat supply device is also communicated with the outside through a heated medium channel to form the first kind of heat-driven compression-absorption heat pump.
10. The first kind of heat-driven compression-absorption heat pump is any one of the first kind of heat-driven compression-absorption heat pumps described in items 6-8, the second throttle valve is eliminated, the heat supply device is added, the third generator is adjusted to be communicated with the condenser through the second throttle valve, the third generator is adjusted to be communicated with the condenser through the heat supply device, and the heat supply device is also communicated with the outside through a heated medium channel to form the first kind of heat-driven compression-absorption heat pump.
11. The first kind of heat-driven compression-absorption heat pump is any one of the first kind of heat-driven compression-absorption heat pumps described in items 2-4 and 9, and the second generator is additionally provided with a high-temperature heat medium channel communicated with the outside to form the first kind of heat-driven compression-absorption heat pump.
12. The first kind of heat-driven compression-absorption heat pump is any one of the first kind of heat-driven compression-absorption heat pumps described in items 6-8 and 10, and the third generator is additionally provided with a high-temperature heat medium channel communicated with the outside to form the first kind of heat-driven compression-absorption heat pump.
13. The first type of thermally driven compression-absorption heat pump according to claim 1, a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added, the generator is adjusted to be communicated with a compressor through a refrigerant steam channel, the generator is communicated with the second absorber through the refrigerant steam channel, the second absorber is also communicated with the second generator through a dilute solution pipeline and the second solution heat exchanger through the second solution pump, the second generator is also communicated with the second absorber through a concentrated solution pipeline and the second solution heat exchanger, the second generator is also communicated with the compressor through the refrigerant steam channel, the second generator is also communicated with the outside through a high-temperature heat medium channel, and the second absorber is also communicated with the outside through a heated medium channel to form a first type of heat-driven compression-absorption heat pump.
14. a first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second solution pump, a second absorber, a solution throttle valve, a second solution throttle valve and a steam-dividing chamber are added in the first kind of heat-driven compression-absorption heat pump described in item 1, the absorber is provided with a dilute solution pipeline which is communicated with the generator through the solution pump and the solution heat exchanger and is adjusted to be that the absorber is provided with a dilute solution pipeline which is communicated with the second absorber through the solution pump and the solution heat exchanger, the second absorber is also provided with a dilute solution pipeline which is communicated with the second generator through the solution throttle valve, the second generator is also provided with a concentrated solution pipeline which is communicated with the generator through the second solution pump, the generator is also adjusted to be that the generator is provided with a concentrated solution pipeline which is communicated with the steam-dividing chamber through the second solution throttle valve and the second absorber, and the steam-dividing chamber is also provided with a concentrated solution pipeline which is communicated with the absorber through, the generator is communicated with the compressor through a refrigerant steam channel, the generator is communicated with a second absorber through the refrigerant steam channel, the second generator and the steam distribution chamber are respectively communicated with the compressor through the refrigerant steam channel, and the second generator is communicated with the outside through a high-temperature heat medium channel to form a first type of heat-driven compression-absorption heat pump.
15. The first kind of heat-driven compression-absorption heat pump is any one of the first kind of heat-driven compression-absorption heat pumps described in items 1-14, wherein a second condenser refrigerant liquid pipeline is communicated with an evaporator through a second refrigerant liquid pump and is adjusted to be communicated with a second condenser refrigerant liquid pipeline through the second refrigerant liquid pump, so that the first kind of heat-driven compression-absorption heat pump is formed.
16. The first kind of heat driven compression-absorption heat pump is one of the first kind of heat driven compression-absorption heat pumps in items 1-15, and has increased power machine connected to the compressor to transmit power to the compressor to form the first kind of heat driven compression-absorption heat pump with additional external power.
17. The first kind of heat driven compression-absorption heat pump is one of the first kind of heat driven compression-absorption heat pumps in items 1-15, and has one working machine added and one expansion machine connected to the working machine to transmit power to the working machine to form the first kind of heat driven compression-absorption heat pump with additional power load.
description of the drawings:
Figure 1 is a schematic diagram of a first principle thermodynamic system of a first type of thermally driven compression-absorption heat pump according to the present invention.
figure 2 is a schematic view of the 2 nd principle thermodynamic system of a first type of thermally driven compression-absorption heat pump according to the present invention.
Figure 3 is a schematic diagram of a principal thermodynamic system of the first type of thermally driven compression-absorption heat pump according to the present invention.
Figure 4 is a diagram of a 4 th principle thermodynamic system for a first type of thermally driven compression-absorption heat pump according to the present invention.
Figure 5 is a diagram of a 5 th principle thermodynamic system for a first type of thermally driven compression-absorption heat pump according to the present invention.
Figure 6 is a 6 th principle thermodynamic system diagram of a first type of thermally driven compression-absorption heat pump provided in accordance with the present invention.
Figure 7 is a 7 th principle thermodynamic system diagram of a first type of thermally driven compression-absorption heat pump provided in accordance with the present invention.
figure 8 is a diagram of a principal thermodynamic system 8 of a first type of thermally driven compression-absorption heat pump according to the present invention.
figure 9 is a diagram of a 9 th principle thermodynamic system of a first type of thermally driven compression-absorption heat pump according to the present invention.
figure 10 is a 10 th principle thermodynamic system diagram of a first type of thermally driven compression-absorption heat pump provided in accordance with the present invention.
Figure 11 is a diagram of a 11 th principle thermodynamic system for a first type of thermally driven compression-absorption heat pump according to the present invention.
in the figure, 1-absorber, 2-generator, 3-compressor, 4-condenser, 5-evaporator, 6-throttle valve, 6-solution pump, 8-solution heat exchanger, 9-refrigerant liquid pump, 10-high temperature heat exchanger, 11-expander, 12-second condenser, 13-second refrigerant liquid pump, 14-second generator, 15-second throttle valve, 16-second solution pump, 17-second solution heat exchanger, 18-second absorber, 19-third generator, 20-third solution pump, 21-third solution heat exchanger, 22-heater, 23-solution throttle valve, 24-second solution throttle valve, 25-steam-dividing chamber.
The specific implementation mode is as follows:
It is to be noted that, in the description of the structure and the flow, the repetition is not necessary; obvious flow is not described. The invention is described in detail below with reference to the figures and examples.
The first type of thermally driven compression-absorption heat pump shown in fig. 1 is implemented as follows:
(1) Structurally, the system mainly comprises an absorber, a generator, a compressor, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a refrigerant liquid pump, a high-temperature heat exchanger, an expander, a second condenser and a second refrigerant liquid pump; the absorber 1 is provided with a dilute solution pipeline which is communicated with the generator 2 through a solution pump 7 and a solution heat exchanger 8, the generator 2 is also provided with a concentrated solution pipeline which is communicated with the absorber 1 through the solution heat exchanger 8, the generator 2 is also provided with a refrigerant steam channel which is communicated with the compressor 3, the compressor 3 is also provided with a refrigerant steam channel which is communicated with the condenser 4, the condenser 4 is also provided with a refrigerant liquid pipeline which is communicated with the evaporator 5 through a throttle valve 6, the condenser 4 is also provided with a refrigerant liquid pipeline which is communicated with the high temperature heat exchanger 10 through a refrigerant liquid pump 9, then the high temperature heat exchanger 10 is further provided with a refrigerant steam channel which is communicated with the expander 11, the expander 11 is also provided with a refrigerant steam channel which is communicated with the second condenser 12, the second condenser 12 is also provided with a refrigerant liquid pipeline which is communicated with the evaporator 5 through a second refrigerant liquid pump 13, the evaporator 5 is also provided with the refrigerant steam channel, the absorber 1 and the condenser 4 are also respectively communicated with the outside through a heated medium channel, the evaporator 5 is also communicated with the outside through a low-temperature heat medium channel, the second condenser 12 is also communicated with the outside through a cooling medium channel, and the expander 11 is connected with the compressor 3 and transmits power.
(2) In the process, dilute solution in the absorber 1 enters the generator 2 through the solution pump 7 and the solution heat exchanger 8, high-temperature heat medium flows through the generator 2, heats the solution entering the generator to release refrigerant steam and provide the refrigerant steam to the compressor 3, and concentrated solution in the generator 2 enters the absorber 1 through the solution heat exchanger 8, absorbs the refrigerant steam and releases heat to the heated medium; refrigerant steam enters the condenser 4 after flowing through the compressor 3 for pressure rise and temperature rise, and releases heat to a heated medium to form refrigerant liquid; the refrigerant liquid of the condenser 4 is divided into two paths, wherein the first path enters the evaporator 5 by throttling through the throttle valve 6, and the second path enters the high-temperature heat exchanger 10 after being pressurized by the refrigerant liquid pump 9, absorbs heat to form refrigerant steam and provides the refrigerant steam to the expansion machine 11; the refrigerant steam flows through the expansion machine 11 to reduce the pressure and do work, the work output by the expansion machine 11 is provided for the compressor 3 to act as the power, the refrigerant steam discharged by the expansion machine 11 enters the second condenser 12 and releases heat to the cooling medium to form refrigerant liquid, and the refrigerant liquid of the second condenser 12 is pressurized by the second refrigerant liquid pump 13 and enters the evaporator 5; the low-temperature heat medium flows through the evaporator 5 and heats the refrigerant liquid entering the evaporator into refrigerant steam, and the refrigerant steam generated by the evaporator 5 is provided for the absorber 1 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in figure 2 is implemented as follows:
(1) structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added, a dilute solution pipeline is additionally arranged on the absorber 1 and is communicated with the second generator 14 through a second solution pump 16 and a second solution heat exchanger 17, a concentrated solution pipeline is further arranged on the second generator 14 and is communicated with the absorber 1 through the second solution heat exchanger 17, a refrigerant steam channel of the generator 2 is communicated with the compressor 3 and is adjusted to be communicated with the second generator 14, then the second generator 14 is communicated with the condenser 4 through the second throttle valve 15, and the second generator 14 is further communicated with the compressor 3 through the refrigerant steam channel.
(2) In the process, refrigerant steam generated by the generator 2 is provided for the second generator 14 to be used as a driving heat medium, part of dilute solution in the absorber 1 enters the second generator 14 through the second solution pump 16 and the second solution heat exchanger 17, the refrigerant steam flows through the second generator 14, heats the solution entering the second generator 14 to release the refrigerant steam and is provided for the compressor 3, and concentrated solution in the second generator 14 enters the absorber 1 through the second solution heat exchanger 17; the refrigerant vapor flowing through the second generator 14 releases heat to form refrigerant liquid, and then enters the condenser 4 through the throttling of the second throttling valve 15 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in figure 3 is implemented as follows:
(1) Structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second throttle valve and a second solution heat exchanger are added, a dilute solution pipeline of an absorber 1 is communicated with a generator 2 through a solution pump 7 and a solution heat exchanger 8 and is adjusted to be communicated with the generator 1, a dilute solution pipeline of the absorber 1 is communicated with the generator 2 through the solution pump 7, the solution heat exchanger 8 and a second solution heat exchanger 17, a concentrated solution pipeline of the generator 2 is communicated with the absorber 1 through the solution heat exchanger 8 and is adjusted to be communicated with the generator 1, a concentrated solution pipeline of the generator 2 is communicated with a second generator 14 through the second solution heat exchanger 17, a concentrated solution pipeline of the second generator 14 is communicated with the absorber 1 through the solution heat exchanger 8, a refrigerant steam channel of the generator 2 is adjusted to be communicated with a compressor 3, a refrigerant steam channel of the generator 2 is communicated with the second generator 14, and a refrigerant liquid pipeline of the second generator 14 is communicated with a condenser 4 through the second throttle valve, the second generator 14 also communicates with the compressor 3 via a refrigerant vapor path.
(2) In the process, refrigerant steam generated by the generator 2 is supplied to the second generator 14 as a driving heat medium, dilute solution in the absorber 1 enters the generator 2 through the solution pump 7, the solution heat exchanger 8 and the second solution heat exchanger 17, concentrated solution in the generator 2 enters the second generator 14 through the second solution heat exchanger 17, the refrigerant steam flows through the second generator 14, heats the solution entering the second generator to release the refrigerant steam and is supplied to the compressor 3, and concentrated solution in the second generator 14 enters the absorber 1 through the solution heat exchanger 8; the refrigerant vapor flowing through the second generator 14 releases heat to form refrigerant liquid, and then enters the condenser 4 through the throttling of the second throttling valve 15 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in fig. 4 is implemented as follows:
(1) Structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added, a dilute solution pipeline of an absorber 1 is communicated with a generator 2 through a solution pump 7 and a solution heat exchanger 8 and is adjusted to be that the absorber 1 is communicated with the second generator 14 through the solution pump 7 and the solution heat exchanger 8, a concentrated solution pipeline of the second generator 14 is communicated with the generator 2 through a second solution pump 16 and a second solution heat exchanger 17, a concentrated solution pipeline of the generator 2 is communicated with the absorber 1 through the solution heat exchanger 8 and is adjusted to be that the generator 2 is communicated with the absorber 1 through the second solution heat exchanger 17 and the solution heat exchanger 8, a refrigerant vapor channel of the generator 2 is communicated with a compressor 3 and is adjusted to be that the generator 2 is communicated with the second generator 14 through a refrigerant vapor channel, and then a refrigerant liquid pipeline of the second generator 14 is adjusted to be communicated with the second generator 2 through the second solution heat exchanger 17 and the solution heat The throttle valve 15 is in communication with the condenser 4 and the second generator 14 is also in communication with the compressor 3 via a refrigerant vapor path.
(2) In the process, refrigerant steam generated by the generator 2 is provided for the second generator 14 to be used as a driving heat medium, dilute solution in the absorber 1 enters the second generator 14 through the solution pump 7 and the solution heat exchanger 8, the refrigerant steam flows through the second generator 14, heats the solution entering the second generator 14 to release the refrigerant steam and provide the refrigerant steam for the compressor 3, concentrated solution in the second generator 14 enters the generator 2 through the second solution pump 16 and the second solution heat exchanger 17, and concentrated solution in the generator 2 enters the absorber 1 through the second solution heat exchanger 17 and the solution heat exchanger 8; the refrigerant vapor flowing through the second generator 14 releases heat to form refrigerant liquid, and then enters the condenser 4 through the throttling of the second throttling valve 15 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in fig. 5 is implemented as follows:
(1) Structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added, a dilute solution pipeline of the absorber 1 is communicated with the generator 2 through the solution pump 7 and the solution heat exchanger 8, the dilute solution pipeline of the absorber 1 is communicated with the second absorber 18 through the solution pump 7 and the solution heat exchanger 8, a dilute solution pipeline of the second absorber 18 is communicated with the generator 2 through the second solution pump 16 and the second solution heat exchanger 17, a concentrated solution pipeline of the generator 2 is communicated with the absorber 1 through the solution heat exchanger 8, the concentrated solution pipeline of the generator 2 is communicated with the second generator 14 through the second solution heat exchanger 17, a concentrated solution pipeline of the second generator 14 is communicated with the generator 1 through the solution heat exchanger 8, a refrigerant steam channel of the second generator 14 is communicated with the second absorber 18, the second generator 14 also has a high-temperature heat medium passage communicating with the outside, and the second absorber 18 also has a heated medium passage communicating with the outside.
(2) In the process, a dilute solution in the absorber 1 enters the second absorber 18 through the solution pump 7 and the solution heat exchanger 8, absorbs refrigerant steam and releases heat to a heated medium, the dilute solution in the second absorber 18 enters the generator 2 through the second solution pump 16 and the second solution heat exchanger 17, a concentrated solution in the generator 2 enters the second generator 14 through the second solution heat exchanger 17, a high-temperature heat medium flows through the second generator 14, heats the solution entering the generator to release the refrigerant steam and is provided for the second absorber 18, and the concentrated solution in the second generator 14 enters the absorber 1 through the solution heat exchanger 8 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in fig. 6 is implemented as follows:
(1) Structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 5, a third generator, a second throttle valve, a third solution pump and a third solution heat exchanger are added, a dilute solution pipeline is additionally arranged on the second absorber 18 and is communicated with the third generator 19 through a third solution pump 20 and a third solution heat exchanger 21, a concentrated solution pipeline is also arranged on the third generator 19 and is communicated with the second generator 14 through the third solution heat exchanger 21, a refrigerant steam channel of the generator 2 is communicated with the compressor 3, the third generator 19 is communicated with the condenser 4 through the second throttle valve 15 after a refrigerant steam channel of the generator 2 is communicated with the third generator 19, and a refrigerant steam channel of the third generator 19 is communicated with the compressor 3.
(2) In the flow, the refrigerant steam generated by the generator 2 is supplied to the third generator 19 as a driving heat medium, part of the dilute solution in the second absorber 18 enters the third generator 19 through the third solution pump 20 and the third solution heat exchanger 21, the refrigerant steam flows through the third generator 19, heats the solution entering the third generator to release the refrigerant steam and is supplied to the compressor 3, and the concentrated solution in the third generator 19 enters the second generator 14 through the third solution heat exchanger 21; the refrigerant vapor flowing through the third generator 19 releases heat to form refrigerant liquid, and then enters the condenser 4 through the throttling of the second throttling valve 15 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in figure 7 is implemented as follows:
(1) structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 5, a third generator, a second throttle valve and a third solution heat exchanger are added, a dilute solution pipeline of a second absorber 18 is communicated with the generator 2 through a second solution pump 16 and a second solution heat exchanger 17, the dilute solution pipeline of the second absorber 18 is adjusted to be communicated with the generator 2 through the second solution pump 16, the second solution heat exchanger 17 and a third solution heat exchanger 21, a concentrated solution pipeline of the generator 2 is communicated with a second generator 14 through the second solution heat exchanger 17, the concentrated solution pipeline of the generator 2 is adjusted to be communicated with the generator 2 through the third solution heat exchanger 21 to be communicated with the third generator 19, a concentrated solution pipeline of the third generator 19 is further communicated with the second generator 14 through the second solution heat exchanger 17, a refrigerant vapor channel of the generator 2 is adjusted to be communicated with a compressor 3, a refrigerant vapor channel of the generator 2 is communicated with the third generator 19, and then the third generator 19 is cooled The refrigerant liquid pipeline is communicated with the condenser 4 through a second throttling valve 15, the third generator 19 is also communicated with the compressor 3 through a refrigerant vapor channel, and the third generator 19 is also communicated with the outside through a high-temperature heat medium channel.
(2) In the process, an external high-temperature heat medium and refrigerant steam generated by the generator 2 are supplied to a third generator 19 as a driving heat medium, a dilute solution in a second absorber 18 enters the generator 2 through a second solution pump 16, a second solution heat exchanger 17 and a third solution heat exchanger 21, a concentrated solution in the generator 2 enters the third generator 19 through the third solution heat exchanger 21, the refrigerant steam and the high-temperature heat medium respectively flow through the third generator 19, the solution entering the third generator is heated to release the refrigerant steam and supply the refrigerant steam to the compressor 3, and the concentrated solution in the third generator 19 enters a second generator 14 through the second solution heat exchanger 17; the refrigerant vapor flowing through the third generator 19 releases heat to form refrigerant liquid, and then enters the condenser 4 through the throttling of the second throttling valve 15 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in fig. 8 is implemented as follows:
(1) Structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 5, a third generator, a second throttle valve, a third solution pump and a third solution heat exchanger are added, a dilute solution pipeline of a second absorber 18 is communicated with a generator 2 through a second solution pump 16 and a second solution heat exchanger 17 and is adjusted to be communicated with the second absorber 18, a dilute solution pipeline of the second absorber 18 is communicated with a third generator 19 through the second solution pump 16 and the second solution heat exchanger 17, a concentrated solution pipeline of the third generator 19 is communicated with the generator 2 through a third solution pump 20 and a third solution heat exchanger 21, a concentrated solution pipeline of the generator 2 is communicated with a second generator 14 through the second solution heat exchanger 17 and is adjusted to be communicated with the generator 2 through a concentrated solution pipeline of the generator 2 through the third solution heat exchanger 21 and the second solution heat exchanger 17 and is adjusted to be communicated with the second generator 14, a refrigerant vapor channel of the generator 2 is communicated with a compressor 3 through a refrigerant vapor channel of the generator 2 and is adjusted to be communicated with the third generator 19 through a refrigerant vapor channel After the communication, the third generator 19 is communicated with the condenser 4 through a second throttling valve 15, and the third generator 19 is communicated with the compressor 3 through a refrigerant steam channel.
(2) in the process, the refrigerant steam generated by the generator 2 is supplied to a third generator 19 as a driving heat medium, the dilute solution of the second absorber 18 enters the third generator 19 through a second solution pump 16 and a second solution heat exchanger 17, the refrigerant steam flows through the third generator 19, heats the solution entering the third generator 19 to release the refrigerant steam and is supplied to the compressor 3, the concentrated solution of the third generator 19 enters the generator 2 through a third solution pump 20 and a third solution heat exchanger 21, and the concentrated solution of the generator 2 enters the second generator 14 through the third solution heat exchanger 21 and the second solution heat exchanger 17; the refrigerant vapor flowing through the third generator 19 releases heat to form refrigerant liquid, and then enters the condenser 4 through the throttling of the second throttling valve 15 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in fig. 9 is implemented as follows:
In the first type of heat-driven compression-absorption heat pump shown in fig. 3, a second throttle valve is eliminated, a heat supply device is added, a refrigerant liquid pipeline of the second generator 14 is communicated with the condenser 4 through the second throttle valve 15, the refrigerant liquid pipeline of the second generator 14 is adjusted to be communicated with the condenser 4 through the heat supply device 22, and the heat supply device 22 is also communicated with the outside through a heated medium channel; the refrigerant vapor passes through the second generator 14 to release heat into refrigerant liquid, the refrigerant liquid passes through the heat supply device 20 and releases heat to the heated medium, and then the refrigerant liquid enters the condenser 4 to form a first type of heat-driven compression-absorption heat pump.
The first type of thermally driven compression-absorption heat pump shown in fig. 10 is implemented as follows:
(1) Structurally, in the first type of thermally driven compression-absorption heat pump shown in fig. 1, a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added, a refrigerant vapor passage of the generator 2 is communicated with the compressor 3 and adjusted to be communicated with the second absorber 18 through the refrigerant vapor passage of the generator 2, the second absorber 18 is further provided with a dilute solution pipeline communicated with the second generator 14 through a second solution pump 16 and a second solution heat exchanger 17, the second generator 14 is further provided with a concentrated solution pipeline communicated with the second absorber 18 through the second solution heat exchanger 17, the second generator 14 is further provided with a refrigerant vapor passage communicated with the compressor 3, the second generator 14 is further provided with a high-temperature heat medium passage communicated with the outside, and the second absorber 18 is further provided with a heated medium passage communicated with the outside.
(2) in the process, refrigerant steam generated by the generator 2 enters the second absorber 18, dilute solution of the second absorber 18 enters the second generator 14 through the second solution pump 16 and the second solution heat exchanger 17, high-temperature heat medium flows through the second generator 14, heats the solution entering the second generator 14 to release the refrigerant steam and provide the refrigerant steam for the compressor 3, and concentrated solution of the second generator 14 enters the second absorber 18 through the second solution heat exchanger 17, absorbs the refrigerant steam and releases heat to the heated medium to form the first type of heat-driven compression-absorption heat pump.
the first type of thermally driven compression-absorption heat pump shown in fig. 11 is implemented as follows:
(1) Structurally, in a first type of thermally driven compression-absorption heat pump shown in figure 1, a second generator, a second solution pump, a second absorber, a solution throttle valve, a second solution throttle valve and a steam distribution chamber are added, wherein a dilute solution pipeline of the absorber 1 is communicated with the generator 2 through a solution pump 7 and a solution heat exchanger 8 and is adjusted to be that the absorber 1 is communicated with a dilute solution pipeline through the solution pump 7 and the solution heat exchanger 8 and is communicated with a second absorber 18, the second absorber 18 is also communicated with a dilute solution pipeline through a solution throttle valve 23 and a second generator 14, the second generator 14 is also communicated with the generator 2 through a concentrated solution pipeline through a second solution pump 16, the generator 2 is adjusted to be communicated with the absorber 1 through the solution heat exchanger 8 and is adjusted to be that the generator 2 is communicated with a concentrated solution pipeline through a second solution throttle valve 24 and a second absorber 18 and is communicated with a steam distribution chamber 25, the steam distribution chamber 25 is also communicated with the absorber 1 through a concentrated solution heat exchanger 8, the generator 2 is adjusted to be communicated with the compressor 3 through a refrigerant steam channel, the generator 2 is communicated with the second absorber 18 through the refrigerant steam channel, the second generator 14 and the steam distribution chamber 25 are further respectively communicated with the compressor 3 through the refrigerant steam channel, and the second generator 14 is further communicated with the outside through a high-temperature heat medium channel.
(2) In the flow, the dilute solution in the absorber 1 enters the second absorber 18 through the solution pump 7 and the solution heat exchanger 8, absorbs refrigerant vapor and releases heat, the dilute solution in the second absorber 18 is throttled by the solution throttle valve 23 and enters the second generator 14, and the high-temperature heat medium flows through the second generator 14, heats the solution entering the second generator 14, releases the refrigerant vapor and provides the refrigerant vapor for the compressor 3; the concentrated solution of the second generator 14 enters the generator 2 through a second solution pump 16, and the concentrated solution of the generator 2 is throttled and depressurized through a second solution throttling valve 24 and then flows through a second absorber 18 to absorb heat and be partially vaporized; the solution after heat absorption and vaporization enters a steam separating chamber 23, the steam separating chamber 23 releases refrigerant steam and provides the refrigerant steam for the compressor 3, and the concentrated solution in the steam separating chamber 23 enters the absorber 1 through the solution heat exchanger 8 to form a first type of heat-driven compression-absorption heat pump.
The effect that the technology of the invention can realize-the first type of thermal drive compression-absorption heat pump provided by the invention has the following effects and advantages:
(1) provides a new idea and a new technology for utilizing the temperature difference.
(2) The heat energy (temperature difference) drives to realize heat supply/refrigeration, or can selectively provide power to the outside at the same time.
(3) The process is reasonable, the performance index is variable, thermodynamic parameter changes are corresponding, and the full and efficient utilization of heat energy (temperature difference) can be realized.
(4) When necessary, heat supply/refrigeration is realized by means of external power, the mode is flexible, and the adaptability is good.
(5) the effective utilization of high-temperature heat energy is realized, the conflict between the parameters of the high-temperature heat medium and the performance of the solution is avoided, and the defects of the absorption heat pump technology are overcome.
(6) Compared with a heat-driven compression heat pump, the flow of the absorption heat pump is adopted to complete refrigerant steam pressure rise, moving parts are reduced, equipment safety is improved, and adverse effects on the environment are reduced.
(7) A plurality of specific technical schemes are provided, so that the method can cope with a plurality of different actual conditions and has a wider application range.
(8) The heat pump technology is expanded, the types of the compression-absorption heat pump are enriched, and the high-efficiency utilization of heat energy is favorably realized.
Claims (17)
1. The first kind of heat-driven compression-absorption heat pump mainly comprises an absorber, a generator, a compressor, a condenser, an evaporator, a throttle valve, a solution pump, a solution heat exchanger, a refrigerant liquid pump, a high-temperature heat exchanger, an expansion machine, a second condenser and a second refrigerant liquid pump; the absorber (1) is provided with a dilute solution pipeline which is communicated with the generator (2) through a solution pump (7) and a solution heat exchanger (8), the generator (2) is also provided with a concentrated solution pipeline which is communicated with the absorber (1) through the solution heat exchanger (8), the generator (2) is also provided with a refrigerant steam channel which is communicated with the compressor (3), the compressor (3) is also provided with a refrigerant steam channel which is communicated with the condenser (4), the condenser (4) is also provided with a refrigerant liquid pipeline which is communicated with the evaporator (5) through a throttle valve (6), the condenser (4) is also provided with a refrigerant liquid pipeline which is communicated with the high temperature heat exchanger (10) through a refrigerant liquid pump (9), then the high temperature heat exchanger (10) is further provided with a refrigerant steam channel which is communicated with the expander (11), the expander (11) is also provided with a refrigerant steam channel which is communicated with a second condenser (12), the second condenser (12) is further provided with a refrigerant liquid pipeline which is communicated with the, the evaporator (5) is also provided with a refrigerant steam channel communicated with the absorber (1), the generator (2) and the high-temperature heat exchanger (10) are also respectively provided with a high-temperature heat medium channel communicated with the outside, the absorber (1) and the condenser (4) are also respectively provided with a heated medium channel communicated with the outside, the evaporator (5) is also provided with a low-temperature heat medium channel communicated with the outside, the second condenser (12) is also provided with a cooling medium channel communicated with the outside, and the expander (11) is connected with the compressor (3) and transmits power to form a first type of heat-driven compression-absorption heat pump; wherein, the expander (11) is connected with the compressor (3), the refrigerant liquid pump (9), the second refrigerant liquid pump (13) and the solution pump (7) and transmits power.
2. A first type of heat-driven compression-absorption heat pump is characterized in that a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added in the first type of heat-driven compression-absorption heat pump as claimed in claim 1, a dilute solution pipeline is additionally arranged on an absorber (1) and is communicated with the second generator (14) through a second solution pump (16) and a second solution heat exchanger (17), the second generator (14) and a concentrated solution pipeline are communicated with the absorber (1) through the second solution heat exchanger (17), a refrigerant steam channel of a generator (2) is communicated with a compressor (3) and adjusted to be communicated with the second generator (14) through a refrigerant steam channel of the generator (2), then the refrigerant liquid pipeline of the second generator (14) is communicated with a condenser (4) through the second throttle valve (15), the refrigerant steam channel of the second generator (14) is communicated with the compressor (3), forming a first type of thermally driven compression-absorption heat pump.
3. a first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second throttle valve and a second solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump as claimed in claim 1, a dilute solution pipeline of an absorber (1) is communicated with a generator (2) through a solution pump (7) and a solution heat exchanger (8) and is adjusted to be communicated with the generator (2) through the solution pump (7), the solution heat exchanger (8) and the second solution heat exchanger (17), a concentrated solution pipeline of the generator (2) is communicated with the absorber (1) through the solution heat exchanger (8) and is adjusted to be communicated with the generator (2) through a concentrated solution pipeline of the generator (2) through the second solution heat exchanger (17) and is communicated with a second generator (14), and the concentrated solution pipeline of the second generator (14) is communicated with the absorber (1) through the solution heat exchanger (8), the generator (2) is communicated with the compressor (3) through a refrigerant steam channel, the generator (2) is adjusted to be communicated with the second generator (14), then the second generator (14) is communicated with the condenser (4) through a second throttling valve (15) through a refrigerant liquid pipeline, and the second generator (14) is also communicated with the compressor (3) through the refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
4. A first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second throttle valve, a second solution pump and a second solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump as claimed in claim 1, a dilute solution pipeline of an absorber (1) is communicated with the generator (2) through the solution pump (7) and the solution heat exchanger (8) and is adjusted to be communicated with the absorber (1) through the solution pump (7) and the solution heat exchanger (8), a dilute solution pipeline of the absorber (1) is communicated with the second generator (14) through the solution pump (7) and the solution heat exchanger (8), a concentrated solution pipeline of the second generator (14) is communicated with the generator (2) through the second solution pump (16) and the second solution heat exchanger (17), a concentrated solution pipeline of the generator (2) is communicated with the absorber (1) through the second solution heat exchanger (17) and the solution heat exchanger (8), the generator (2) is communicated with the compressor (3) through a refrigerant steam channel, the generator (2) is adjusted to be communicated with the second generator (14), then the second generator (14) is communicated with the condenser (4) through a second throttling valve (15) through a refrigerant liquid pipeline, and the second generator (14) is also communicated with the compressor (3) through the refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
5. A first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump as claimed in claim 1, a dilute solution pipeline of the absorber (1) is communicated with the generator (2) through the solution pump (7) and the solution heat exchanger (8) and is adjusted to be communicated with the absorber (1) through the solution pump (7) and the solution heat exchanger (8), the dilute solution pipeline of the second absorber (18) is communicated with the generator (2) through the second solution pump (16) and the second solution heat exchanger (17), a concentrated solution pipeline of the generator (2) is communicated with the absorber (1) through the solution heat exchanger (8) and is adjusted to be communicated with the generator (2) through the second solution heat exchanger (17) and the second generator (14), the second generator (14) is communicated with the absorber (1) through a concentrated solution pipeline through a solution heat exchanger (8), the second generator (14) is also communicated with a second absorber (18) through a refrigerant steam channel, the second generator (14) is also communicated with the outside through a high-temperature heat medium channel, and the second absorber (18) is also communicated with the outside through a heated medium channel to form a first type of heat-driven compression-absorption heat pump.
6. A first type of heat-driven compression-absorption heat pump is characterized in that a third generator, a second throttle valve, a third solution pump and a third solution heat exchanger are added in the first type of heat-driven compression-absorption heat pump as claimed in claim 5, a dilute solution pipeline is additionally arranged on a second absorber (18) and is communicated with the third generator (19) through a third solution pump (20) and a third solution heat exchanger (21), the third generator (19) and a concentrated solution pipeline are communicated with the second generator (14) through the third solution heat exchanger (21), the generator (2) is communicated with the compressor (3) through a refrigerant steam channel, the third generator (19) is communicated with the condenser (4) through the second throttle valve (15) after the generator (2) is communicated with the third generator (19) through the refrigerant steam channel, the third generator (19) is also communicated with the compressor (3) through the refrigerant steam channel, forming a first type of thermally driven compression-absorption heat pump.
7. A first kind of heat-driven compression-absorption heat pump is characterized in that a third generator, a second throttle valve and a third solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump as claimed in claim 5, a dilute solution pipeline of a second absorber (18) is communicated with the generator (2) through a second solution pump (16) and a second solution heat exchanger (17) and is adjusted to be communicated with the generator (2) through the second solution pump (16), the second solution heat exchanger (17) and the third solution heat exchanger (21), a concentrated solution pipeline of the generator (2) is communicated with the second generator (14) through the second solution heat exchanger (17) and is adjusted to be communicated with the generator (2) through a concentrated solution pipeline of the generator (2) through the third solution heat exchanger (21) and is communicated with the third generator (19), and the concentrated solution pipeline of the third generator (19) is communicated with the second generator (14) through the second solution heat exchanger (17), the generator (2) is communicated with the compressor (3) through a refrigerant steam channel, the generator (2) is adjusted to be communicated with the third generator (19), then the third generator (19) is communicated with the condenser (4) through a second throttling valve (15) through a refrigerant liquid pipeline, and the third generator (19) is also communicated with the compressor (3) through the refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
8. A first kind of heat-driven compression-absorption heat pump is characterized in that a third generator, a second throttle valve, a third solution pump and a third solution heat exchanger are added in the first kind of heat-driven compression-absorption heat pump as set forth in claim 5, a dilute solution pipeline of a second absorber (18) is communicated with the generator (2) through a second solution pump (16) and a second solution heat exchanger (17) and is adjusted to be communicated with the second absorber (18) through the second solution pump (16) and the second solution heat exchanger (17), a dilute solution pipeline of the third generator (19) is communicated with the generator (2) through the second solution pump (16) and the second solution heat exchanger (17), a concentrated solution pipeline of the generator (2) is communicated with the generator (2) through a third solution pump (20) and the third solution heat exchanger (21), a concentrated solution pipeline of the generator (2) is communicated with the second generator (14) through the second solution heat exchanger (17) and is adjusted to be communicated with the generator (2) through a concentrated solution pipeline through the third solution heat exchanger (21) and the second solution heat exchanger (14) (17) The generator (2) is communicated with the compressor (3) through a refrigerant steam channel, the generator (2) is adjusted to be communicated with the compressor (3) through the refrigerant steam channel, then the third generator (19) is communicated with the condenser (4) through a second throttling valve (15) after the generator (2) is communicated with the third generator (19), and the third generator (19) is also communicated with the compressor (3) through the refrigerant steam channel to form a first type of heat-driven compression-absorption heat pump.
9. The first kind of heat-driven compression-absorption heat pump is the first kind of heat-driven compression-absorption heat pump as set forth in any one of claims 2 to 4, a second throttle valve is eliminated, a heat supply device is added, a refrigerant liquid pipeline of the second generator (14) is communicated with the condenser (4) through the second throttle valve (15) and adjusted to be communicated with the condenser (4) through the heat supply device (22) and the refrigerant liquid pipeline of the second generator (14), and the heat supply device (22) is also communicated with the outside through a heated medium channel to form the first kind of heat-driven compression-absorption heat pump.
10. The first kind of heat-driven compression-absorption heat pump is the first kind of heat-driven compression-absorption heat pump as set forth in any one of claims 6 to 8, the second throttle valve is eliminated, the heat supply device is added, the refrigerant liquid pipeline of the third generator (19) is communicated with the condenser (4) through the second throttle valve (15) and adjusted to be communicated with the condenser (4) through the heat supply device (22) and the refrigerant liquid pipeline of the third generator (19), and the heat supply device (22) and the heated medium channel are communicated with the outside to form the first kind of heat-driven compression-absorption heat pump.
11. The first kind of heat-driven compression-absorption heat pump is any one of the first kind of heat-driven compression-absorption heat pumps in claims 2-4 and 9, and the second generator (14) is additionally provided with a high-temperature heat medium channel communicated with the outside to form the first kind of heat-driven compression-absorption heat pump.
12. The first kind of heat-driven compression-absorption heat pump is the first kind of heat-driven compression-absorption heat pump as claimed in any one of claims 6-8 and 10, and the third generator (19) is additionally provided with a high-temperature heat medium channel communicated with the outside to form the first kind of heat-driven compression-absorption heat pump.
13. A first type of heat-driven compression-absorption heat pump is characterized in that a second generator, a second absorber, a second solution pump and a second solution heat exchanger are added in the first type of heat-driven compression-absorption heat pump as claimed in claim 1, a generator (2) is communicated with a compressor (3) through a refrigerant steam channel and adjusted to be communicated with the second absorber (18) through the refrigerant steam channel of the generator (2), the second absorber (18) is also communicated with a dilute solution pipeline through a second solution pump (16) and a second solution heat exchanger (17) and a second generator (14), the second generator (14) is also communicated with the second absorber (18) through a second solution heat exchanger (17), the second generator (14) is also communicated with the compressor (3) through the refrigerant steam channel, and the second generator (14) is also communicated with the outside through a high-temperature heat medium channel, the second absorber (18) is also communicated with the outside by a heated medium channel to form a first type of heat-driven compression-absorption heat pump.
14. A first kind of heat-driven compression-absorption heat pump is characterized in that a second generator, a second solution pump, a second absorber, a solution throttle valve, a second solution throttle valve and a steam distribution chamber are added in the first kind of heat-driven compression-absorption heat pump as claimed in claim 1, a dilute solution pipeline of the absorber (1) is communicated with the generator (2) through a solution pump (7) and a solution heat exchanger (8) and is adjusted to be communicated with the absorber (1) through the solution pump (7) and the solution heat exchanger (8), a dilute solution pipeline of the second absorber (18) is communicated with the second generator (14) through a solution throttle valve (23), a concentrated solution pipeline of the second generator (14) is communicated with the generator (2) through a second solution pump (16), a concentrated solution pipeline of the generator (2) is communicated with the absorber (1) through the solution heat exchanger (8) and is adjusted to be communicated with the generator (2) through a concentrated solution pipeline of the second solution heat exchanger (8) The liquid throttle valve (24) and the second absorber (18) are communicated with the steam distribution chamber (25), the steam distribution chamber (25) is further communicated with the absorber (1) through a concentrated solution pipeline through a solution heat exchanger (8), the generator (2) is communicated with the compressor (3) through a refrigerant steam channel, the generator (2) is adjusted to be communicated with the second absorber (18) through the refrigerant steam channel, the second generator (14) and the steam distribution chamber (25) are further communicated with the compressor (3) through the refrigerant steam channel respectively, and the second generator (14) is further communicated with the outside through a high-temperature heat medium channel to form a first-type heat-driven compression-absorption heat pump.
15. The first kind of heat-driven compression-absorption heat pump is the first kind of heat-driven compression-absorption heat pump as set forth in any one of claims 1 to 14, wherein the refrigerant liquid pipeline of the second condenser (12) is communicated with the evaporator (5) through the second refrigerant liquid pump (13) and is adjusted to be communicated with the condenser (4) through the second refrigerant liquid pump (13) to form the first kind of heat-driven compression-absorption heat pump.
16. The first kind of heat-driven compression-absorption heat pump is the first kind of heat-driven compression-absorption heat pump which is added with a power machine in any one of the first kind of heat-driven compression-absorption heat pumps in the claims 1 to 15, wherein the power machine is connected with the compressor (3) and transmits power to the compressor (3) to form additional external power driven first kind of heat-driven compression-absorption heat pump.
17. The first kind of heat-driven compression-absorption heat pump is the first kind of heat-driven compression-absorption heat pump which is added with a working machine in any one of the first kind of heat-driven compression-absorption heat pumps in claims 1-15, and an expansion machine (11) is connected with the working machine and transmits power to the working machine to form an additional externally-supplied power load.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510381690 | 2015-06-28 | ||
| CN2015103816904 | 2015-06-28 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106225302A CN106225302A (en) | 2016-12-14 |
| CN106225302B true CN106225302B (en) | 2019-12-13 |
Family
ID=57519627
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610522622.XA Active CN106225302B (en) | 2015-06-28 | 2016-06-27 | First-class thermally driven compression-absorption heat pump |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106225302B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001099520A (en) * | 1999-09-29 | 2001-04-13 | Osaka Gas Co Ltd | Hybrid absorbing type electrical power and cold heat or hot heat supplying device |
| JP2010048446A (en) * | 2008-08-20 | 2010-03-04 | Ntn Corp | Hybrid air cycle refrigerating and cooling unit |
| CN102410660A (en) * | 2011-10-25 | 2012-04-11 | 浙江理工大学 | Absorption-compression-type dual-purpose second species heat pump system |
| CN104567093A (en) * | 2014-12-26 | 2015-04-29 | 华电电力科学研究院 | Afterheat recycling method and device for steam driving type tandem type heat pumps |
-
2016
- 2016-06-27 CN CN201610522622.XA patent/CN106225302B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001099520A (en) * | 1999-09-29 | 2001-04-13 | Osaka Gas Co Ltd | Hybrid absorbing type electrical power and cold heat or hot heat supplying device |
| JP2010048446A (en) * | 2008-08-20 | 2010-03-04 | Ntn Corp | Hybrid air cycle refrigerating and cooling unit |
| CN102410660A (en) * | 2011-10-25 | 2012-04-11 | 浙江理工大学 | Absorption-compression-type dual-purpose second species heat pump system |
| CN104567093A (en) * | 2014-12-26 | 2015-04-29 | 华电电力科学研究院 | Afterheat recycling method and device for steam driving type tandem type heat pumps |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106225302A (en) | 2016-12-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108679880B (en) | Double-working medium combined cycle compression heat pump | |
| CN106440510B (en) | Second-class thermally-driven compression heat pump | |
| CN106016821B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106440493B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN106322821B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN106568233B (en) | Third-class thermally-driven compression heat pump | |
| CN105953464B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN106247674B (en) | First-class thermally driven compression-absorption heat pump | |
| CN105841401B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106369870B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN105953467B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN105953465B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN106247653B (en) | First-class thermally-driven compression heat pump | |
| CN106440498B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN106440494B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN105928246B (en) | Fifth type thermal driving compression-absorption heat pump | |
| CN106196710B (en) | First-class thermally driven compression-absorption heat pump | |
| CN105910341B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106440491B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106440495B (en) | Fourth type thermal driving compression-absorption heat pump | |
| CN106225302B (en) | First-class thermally driven compression-absorption heat pump | |
| CN105953463B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106225303B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106196711B (en) | First-class thermally driven compression-absorption heat pump | |
| CN106440509B (en) | Third-class thermally-driven compression heat pump |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |