CN216240842U - Low-temperature circulating power generation system using carbon dioxide gas as working medium - Google Patents
Low-temperature circulating power generation system using carbon dioxide gas as working medium Download PDFInfo
- Publication number
- CN216240842U CN216240842U CN202122766995.0U CN202122766995U CN216240842U CN 216240842 U CN216240842 U CN 216240842U CN 202122766995 U CN202122766995 U CN 202122766995U CN 216240842 U CN216240842 U CN 216240842U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- power generation
- heat
- generation system
- low
- 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
Images
Landscapes
- Treating Waste Gases (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
The utility model discloses a low-temperature circulating power generation system using carbon dioxide gas as a working medium. The utility model adopts 2-methylimidazole aqueous solution to absorb CO at low temperature (20-40 ℃) and low pressure (0.2-0.3 MPa)2Absorbing heat at a higher temperature (80-120 ℃) and releasing high-pressure (0.8-1.2 MPa) CO2And the gas is expanded by a turbine to do work externally to generate electricity. Due to CO2The desorption temperature is about 80 ℃, so that solar hot water, terrestrial heat or low-temperature waste heat of factories can be utilized for the desorptionThe heat source for desorption realizes low-temperature circulating power generation.
Description
Technical Field
The utility model relates to the technical field of low-grade heat energy power generation, in particular to a low-temperature circulating power generation system taking carbon dioxide gas as a working medium.
Background
At present, the most widely applied power generation method is a Rankine cycle, but in practical application, the following two problems mainly exist. Firstly, because the circulating medium mostly adopts low boiling point compounds, a condenser and an evaporator are needed to be arranged to lead the working medium to generate phase change, the consumed energy is more, and the heat load of the equipment is larger. On the other hand, in order to improve the thermal efficiency of the Rankine cycle, a reheater is often introduced to realize a secondary isobaric heating process, and superheated steam enables investment cost of high-temperature-resistant equipment such as a superheater and a turbine to be higher.
2-methylimidazole belongs to imidazole compounds, has a boiling point of 267 ℃, is widely applied to the fields of corrosion inhibitors, gas separation and the like due to the properties of low toxicity, high chemical stability, low production cost and the like, and is often used as a ligand to synthesize zeolite imidazole materials (ZIFs). 2-methylimidazole-CO2The gas has good absorption performance, so the gas can be used as CO2Absorbent of gases, in addition to CO in solution at higher temperatures (about 80 ℃ C.)2A desorption process can occur to achieve the recyclable use of the absorbent. The utility model utilizes low-grade heat energy, such as solar energy, geothermal energy, factory low-temperature waste heat and the like, only needs to transmit less mechanical energy for fluid, can greatly reduce the energy consumption of low-temperature power generation circulation, and has the advantages of safety, environmental protection, stable operation, high heat efficiency and the like.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a catalyst prepared from CO2Is a low-temperature circulating power generation system of working media. The low temperatureThe circulating power generation system provides heat by using low-grade heat energy, and the 2-methylimidazole water solution provides CO2Compared with the traditional low-temperature Rankine cycle power generation, the low-grade heat source system can realize the efficient utilization of solar hot water, geothermal energy, factory waste heat and other low-grade heat sources, and integrally improves the stability and the efficiency of the system.
In order to achieve the purpose, the utility model adopts the following technical scheme:
the utility model provides a low-temperature circulating power generation system using carbon dioxide gas as a working medium, which comprises:
CO2absorption unit, first heat exchanger, circulation booster pump, CO2Desorption unit, CO2Turbines, generators;
the CO is2The outlet of the absorption unit is connected with the inlet of the circulating booster pump after passing through the first heat exchanger, and the outlet of the circulating booster pump is connected with the CO2Inlet connection of desorption unit, CO2The liquid outlet of the desorption unit passes through the first heat exchanger and then is connected with the CO2The inlet of the absorption unit is connected; the CO is2Gas outlet of desorption unit and said CO2Inlet connection of a turbine, said CO2Outlet of the turbine and said CO2Inlet connection of an absorption unit, and the CO2The turbine is connected with the generator; the CO is2The desorption unit is provided with a heating device;
the carbon dioxide gas is in the CO2Absorption unit, first heat exchanger, circulation booster pump, CO2Desorption unit and CO2Circulation between turbines;
the low-temperature circulating power generation system adopts 2-methylimidazole water solution as an absorption medium of carbon dioxide gas, wherein CO is absorbed by the carbon dioxide gas2Absorption unit, first heat exchanger, circulation booster pump, CO2Circulating among the desorption units.
According to the low-temperature cycle power generation system of the present invention, preferably, the heating device is connected to an apparatus for providing a low-grade heat source.
According to the low-temperature cycle power generation system of the utility model, preferably, the device for providing the low-grade heat source is selected from a solar water heater, a geothermal device or a factory low-temperature waste heat device. The low-grade heat source is selected from solar hot water, geothermal heat or low-temperature waste heat of a factory. For example, the heating device is a water heater, and the heat source for heating water is a low-grade heat source such as solar hot water, geothermal heat, or low-temperature waste heat of a factory; the hot water in the heating device is the CO through a heating coil2The desorption unit provides heat. When solar water is adopted, the heating device is a solar water heater.
According to the low temperature cycle power generation system of the present invention, preferably, the CO2The absorption unit is provided with an external heat collector for removing the absorption heat of the reaction in time to enable CO to be absorbed2The temperature of the system is stable in the absorption process.
According to the low-temperature cycle power generation system of the utility model, preferably, the internal heat-taking medium of the external heat collector is cooling water.
According to the low-temperature cycle power generation system, preferably, the first heat exchanger is a shell-and-tube heat exchanger; the CO is2An outlet of the absorption unit is connected with a tube pass inlet of the first heat exchanger, and a tube pass outlet of the first heat exchanger is connected with an inlet of the circulating booster pump; the CO is2A liquid outlet of the desorption unit is connected with a shell-side inlet of the heat exchanger, and a shell-side outlet of the first heat exchanger is connected with the CO2The inlets of the absorption units are connected.
That is, the tube side of the first heat exchanger is rich liquid (rich CO)2The 2-methylimidazole aqueous solution) of (a) and the shell side is a barren solution (also called desorption solution); where they exchange heat.
According to the low-temperature cycle power generation system, preferably, the low-temperature cycle power generation system further comprises a second heat exchanger, and the shell side outlet of the first heat exchanger passes through the second heat exchanger and then is connected with the CO2The inlets of the absorption units are connected. And the lean solution is subjected to heat exchange with the rich solution through the first heat exchanger and is cooled through the second heat exchanger.
According to the low-temperature cycle power generation system of the utility model, preferably, the internal heat exchange medium of the second heat exchanger is cooling water.
According to the low temperature cycle power generation system of the present invention, preferably, the CO2A pressure reducing valve is arranged on a connecting pipeline between a liquid outlet of the desorption unit and the first heat exchanger; the CO is2The lean solution desorbed in the desorption unit is decompressed by the pressure reducing valve, cooled by the first heat exchanger and the second heat exchanger and then returns to the CO2An absorption unit.
In a preferred embodiment of the present invention, the low-temperature cycle power generation system further includes a second heat exchanger and a pressure reducing valve, and the first heat exchanger is a shell-and-tube heat exchanger;
the CO is2An outlet of the absorption unit is connected with a tube pass inlet of the first heat exchanger, and a tube pass outlet of the first heat exchanger is connected with an inlet of the circulating booster pump;
the CO is2A liquid outlet of the desorption unit is connected with a shell pass inlet of the heat exchanger after passing through the pressure reducing valve, and a shell pass outlet of the first heat exchanger is connected with the CO2The inlets of the absorption units are connected.
CO with the Low temperature cycle Power Generation System of the present invention2The low-temperature circulating power generation method of the working medium comprises the following steps:
in the CO2CO absorption by 2-methylimidazole aqueous solution in absorption unit2The gas becomes rich liquid, and the rich liquid enters the CO after being subjected to pressure boosting after being subjected to heat exchange and temperature rise with the barren solution through the first heat exchanger2A desorption unit;
the low-grade heat source is the CO2The desorption unit supplies heat to make CO2The gas is desorbed from the rich solution and enters the CO2The turbine expands to do work and drives the generator to generate electricity; the desorbed barren solution is cooled by the first heat exchanger and rich solution to return to the CO2An absorption unit.
In the low temperature cycle power generation method, preferably, the CO is used2The operation temperature of the absorption unit is 20-40 ℃, and the operation is carried outThe pressure is 0.2-0.3 MPa.
In the low temperature cycle power generation method, preferably, the CO is used2The operating temperature of the desorption unit is 80-120 ℃, and the operating pressure is 0.8-1.2 MPa; and pressurizing the rich solution to 0.8-1.2 MPa by a circulating booster pump.
In the low-temperature cycle power generation method, the concentration of the 2-methylimidazole aqueous solution is preferably 30-60 wt.%.
In the low temperature cycle power generation method, preferably, the CO is used2The outlet pressure of the turbine is 0.2-0.3 MPa.
The low-temperature circulating power generation system using carbon dioxide gas as the working medium provided by the utility model adopts 2-methylimidazole water solution to absorb CO at low temperature (20-40 ℃) and low pressure (0.2-0.3 MPa)2Absorbing heat at a higher temperature (80-120 ℃) and releasing high-pressure (0.8-1.2 MPa) CO2And the gas is expanded by a turbine to do work externally to generate electricity. Due to CO2The desorption temperature of the device is about 80 ℃, so that solar hot water, terrestrial heat or low-temperature waste heat of a factory can be used as a heat source for desorption, and low-temperature position cycle power generation is realized. The system of the utility model uses CO2The working medium is 2-methylimidazole water solution, the absorbing medium is 2-methylimidazole water solution, low-grade heat sources such as solar hot water, terrestrial heat and factory waste heat are utilized to generate electricity, and energy conservation and carbon emission reduction are realized. Due to CO2The cycle is non-toxic, non-flammable and non-explosive, is safer and more environment-friendly than the existing low-temperature organic Rankine cycle, and has higher thermoelectric efficiency.
Drawings
Fig. 1 is a schematic diagram of a low-temperature cycle power generation system using carbon dioxide gas as a working medium in a preferred embodiment of the present invention.
FIG. 2 is a schematic diagram of an offshore solar-powered carbon dioxide gas cycle power generation system in a preferred embodiment of the utility model.
Description of reference numerals:
1 CO2absorption unit
2 first heat exchanger
3 circulation booster pump
4 CO2Desorption unit
5 second heat exchanger
6 CO2Turbine machine
7 electric generator
8 pressure reducing valve
9 valve
10 solar water heater
11 external heat collector
Detailed Description
In order to more clearly illustrate the utility model, the utility model is further described below in connection with preferred embodiments. It is to be understood by persons skilled in the art that the following detailed description is illustrative and not restrictive, and is not to be taken as limiting the scope of the utility model.
The utility model provides a preferred embodiment, as shown in fig. 1, a low-temperature cycle power generation system using carbon dioxide gas as a working medium, wherein the low-temperature cycle power generation system adopts CO2The gas is used as a circulating working medium, and the 2-methylimidazole water solution is used as an absorption medium, and the method comprises the following steps: CO 22Absorption unit 1, first heat exchanger 2, circulating booster pump 3, CO2Desorption unit 4, second heat exchanger 5, CO2A turbine 6 and a generator 7.
The CO is2The outlet of the absorption unit 1 is connected with the inlet of the circulating booster pump 3 after passing through the first heat exchanger 2, and the outlet of the circulating booster pump 3 is connected with the CO2Inlet connection of desorption unit 4, said CO2The liquid outlet of the desorption unit 4 is connected with the CO after passing through the first heat exchanger 2 and the second heat exchanger 52The inlet of the absorption unit 1 is connected; the CO is2Gas outlet of desorption unit 4 and the CO2Inlet connection of a turbine 6, said CO2Outlet of turbine 6 and said CO2The inlet of the absorption unit 1 is connected, and the CO2The turbine 6 is connected with the generator 7; the CO is2The desorption unit 4 is provided with a heating device for providing heat for the desorption of the rich liquid, and the heating device provides heat from a low-grade heat source. The low-grade heat source is selected from solar energy, geothermal energy or low-temperature waste heat of a factory.
Furthermore, the CO2The absorption unit 1 is provided with an external heat collector 11 for removing the heat of absorption of the reaction in time to make the CO react2The temperature of the system is stable in the absorption process. The heat-taking medium in the external heat collector 11 is cooling water. The internal heat exchange medium of the second heat exchanger 5 is also cooling water.
In particular, the CO is2An outlet of the absorption unit 1 is connected with a tube pass inlet of the first heat exchanger 2, and a tube pass outlet of the first heat exchanger 2 is connected with an inlet of the circulating booster pump 3; the CO is2A liquid outlet of the desorption unit 4 is connected with a shell pass inlet of the heat exchanger 2, a shell pass outlet of the first heat exchanger 2 is connected with an inlet of the second heat exchanger 5, and an outlet of the second heat exchanger 5 is connected with CO2The inlets of the absorption units 1 are connected. Namely, the tube side of the first heat exchanger 2 is rich liquid, and the shell side is lean liquid; where they exchange heat.
Further, said CO2A pressure reducing valve 8 is arranged on a connecting pipeline between a liquid outlet of the desorption unit 4 and the first heat exchanger 2; the CO is2The lean solution desorbed in the desorption unit 4 is decompressed by the decompression valve 8, cooled by the first heat exchanger 2 and the second heat exchanger 5, and returned to the CO2An absorption unit 1.
The process of cyclic power generation using the system of fig. 1 includes:
in the 2-methylimidazole water solution circulation loop, CO2CO absorption by 2-methylimidazole aqueous solution in absorption unit 12The gas becomes rich liquid (rich in CO)2The absorption liquid) and the lean liquid (also called desorption liquid) through a first heat exchanger 2, and the rich liquid is compressed and boosted through a circulating booster pump 3 and then enters CO2Desorption unit 4 for CO2While low grade heat sources such as solar hot water, geothermal energy and plant waste heat are passed through CO2For which the heating means of the desorption unit 4 are providedHeat supply. Lean solution of CO2The liquid outlet of the desorption unit 4 is further cooled by a pressure reducing valve 8, the first heat exchanger 2 and the second heat exchanger 5, and finally conveyed to CO2Absorption Unit 1 for CO2The gas absorption process, the heat generated in the absorption process is removed by the external heat collector 11 in time to keep the temperature of the system stable. Rich solution in CO2After desorption in the desorption unit 4, CO2The gas is composed of CO2The top gas outlet of the desorption unit 4 enters CO through a pipeline2The turbine 6 performs an expansion work process, and the generator 7 meets the power generation requirement of the circulating device. Expanded CO2Gas return to CO2And the absorption unit 1 completes low-temperature power generation circulation.
Wherein said CO is2The operation temperature of the absorption unit 1 is 20-40 ℃, and the operation pressure is 0.2-0.3 MPa. The CO is2The operating temperature of the desorption unit 4 is 80-120 ℃, and the operating pressure is 0.8-1.2 MPa. The concentration of the 2-methylimidazole aqueous solution is 30-60 wt.%. CO 22The outlet pressure of the turbine 6 is 0.2 to 0.3 MPa.
Application example 1
The application scenario of the application example is that the carbon dioxide gas driven by the offshore solar energy is used for cyclic power generation, and the adopted gaseous cyclic working medium is CO2，CO2Absorption unit 1 and CO2The solution in the desorption unit 4 is 30-60 wt.% of 2-methylimidazole water solution, and the heat exchange and heat extraction device has seawater as an internal medium.
As shown in FIG. 2, the recycle system of the present application example includes CO2Absorption unit 1, first heat exchanger 2, circulating booster pump 3, CO2Desorption unit 4, second heat exchanger 5, CO2A turbine 6, a generator 7, a solar water heater 10 and an external heat collector 11.
CO2The outlet of the absorption unit 1 is connected with the tube side inlet of the first heat exchanger 2, and the tube side outlet of the first heat exchanger 2 is connected with CO through a circulating booster pump 32The inlets of the desorption units 4 are connected, CO2The liquid outlet of the desorption unit 4 passes through the shell side of the first heat exchanger 2 and the second heat exchanger 5 and the CO2The inlets of the absorption units 1 are connected. With CO2Gas outlet of desorption unit 4 and CO2Inlet of turbine 6 connected to CO2The turbine 6 is connected to a generator 7, the expanded CO2Gas return to CO2And the absorption unit 1 completes power circulation. Outlet of solar water heater 10 and CO2The heating coil inlet arranged on the desorption unit 4 is connected to complete heat supply for the desorption unit, and a valve 9 is arranged on the connecting pipeline. CO 22The absorption unit 1 is provided with an external heat remover 11.
The circulating booster pump 3 boosts the pressure of the rich solution from 0.2-0.3 MPa to 0.8-1.2 MPa. Through the first heat exchanger 2 and CO2Heating the rich solution to 80-120 ℃ by a heating coil of the desorption unit 4, and heating CO2The absorption temperature in the absorption unit 1 is maintained at 20-40 ℃.
The carbon dioxide gas cycle power generation process based on solar energy by using the system of the application example comprises the following steps:
the solar water heater heats water in the internal storage tank, and hot water passes through CO from the water heater2The heating coil arranged in the desorption unit 4 exchanges heat with the internal solution, and hot water after heat exchange returns to the water heater to realize CO2Heat supply to the desorption unit 4. CO 22After heating the rich liquid in the desorption unit 4, CO2Desorbing and escaping from the rich solution, circulating the system with CO2The gas is used as a circulating working medium. Gaseous CO2Into CO2The turbine 6 works to drive the generator 7 to generate electricity. The barren solution is decompressed by a decompression valve 8, the first heat exchanger 2 exchanges heat with the rich solution, the second heat exchanger 5 exchanges heat with the seawater and returns to the CO2Absorption Unit 1, external Heat collector 11 for timely CO removal2The heat of reaction in the unit 1 is absorbed.
CO2The gas returns to CO after expanding and doing work2Absorption unit 1, CO2The gas is bubbled with CO2The lean solution sprayed above the absorption unit 1 is subjected to gas-liquid mass transfer, and CO is carried out in the absorption unit2The absorption process of (1). The rich liquid is boosted by the circulating booster pump 3 and then returns to CO2And a desorption unit 4 for completing the power generation cycle.
In addition, in the application example, the seawater storage is huge, the temperature is low, the temperature fluctuation is small, the seawater storage is an ideal low-temperature cold source, the system does not need to depend on other related project construction, and the economic investment is low.
Application example 2
The solar-energy-based carbon dioxide gas circulation power generation device and the method provided by the application example have the same structure as the application example 1, and the difference is that the second heat exchanger 5 and the external heat collector 11 have large lake water or cold air as internal media.
Application example 3
The low-temperature circulating power generation device and method provided by the application example are basically the same as the application example 2 in structure, and the difference lies in that CO2The heat of the heating device provided in the desorption unit 4 is supplied by low-temperature geothermal heat or plant waste heat.
In the above embodiments and application examples of the present invention, the CO2The absorption unit 1 may be CO2Absorption tanks or CO2Absorption column of said CO2The desorption units 4 can also each be CO2Desorption tanks or CO2The desorption tower and the specific equipment can be arranged according to requirements.
It should be understood that the above-mentioned embodiments of the present invention are only examples for clearly illustrating the present invention, and are not intended to limit the embodiments of the present invention, and it will be obvious to those skilled in the art that other variations or modifications may be made on the basis of the above description, and all embodiments may not be exhaustive, and all obvious variations or modifications may be included within the scope of the present invention.
Claims (10)
1. A low-temperature cycle power generation system using carbon dioxide gas as a working medium is characterized by comprising:
CO2an absorption unit (1), a first heat exchanger (2), a circulating booster pump (3), and CO2Desorption unit (4), CO2A turbine (6), a generator (7);
the CO is2The outlet of the absorption unit (1) is connected with the inlet of the circulating booster pump (3) after passing through the first heat exchanger (2), and the circulation is carried outAn outlet of the ring booster pump (3) and the CO2Inlet connection of desorption unit (4), CO2A liquid outlet of the desorption unit (4) passes through the first heat exchanger (2) and then is connected with the CO2The inlets of the absorption units (1) are connected; the CO is2A gas outlet of the desorption unit (4) and the CO2Inlet connection of a turbine (6), said CO2An outlet of the turbine (6) and the CO2The inlets of the absorption units (1) are connected, and the CO2The turbine (6) is connected with the generator (7); the CO is2The desorption unit (4) is provided with a heating device;
the carbon dioxide gas is in the CO2An absorption unit (1), a first heat exchanger (2), a circulating booster pump (3), and CO2A desorption unit (4) and CO2Circulating between the turbines (6);
the low-temperature circulating power generation system adopts 2-methylimidazole water solution as an absorption medium of carbon dioxide gas, wherein CO is absorbed by the carbon dioxide gas2An absorption unit (1), a first heat exchanger (2), a circulating booster pump (3), and CO2Circulating among the desorption units (4).
2. The cryogenic cycle power generation system of claim 1, wherein the heating device is connected to a device that provides a low grade heat source.
3. A cryogenic cycle power generation system according to claim 2 wherein the means to provide a low grade heat source is selected from a solar water heater, a geothermal plant or a plant low temperature waste heat plant.
4. The cryogenic cycle power generation system of claim 1, wherein the CO is2The absorption unit (1) is provided with an external heat collector (11).
5. A cryogenic cycle power generation system according to claim 4, wherein the internal heat taking medium of the external heat collector (11) is cooling water.
6. According to the rightThe cryogenic cycle power generation system of claim 1, wherein the first heat exchanger (2) is a shell and tube heat exchanger; the CO is2An outlet of the absorption unit (1) is connected with a tube-side inlet of the first heat exchanger (2), and a tube-side outlet of the first heat exchanger (2) is connected with an inlet of the circulating booster pump (3);
the CO is2A liquid outlet of the desorption unit (4) is connected with a shell-side inlet of the heat exchanger (2), and a shell-side outlet of the first heat exchanger (2) is connected with the CO2The inlets of the absorption units (1) are connected.
7. The cryogenic cycle power generation system of claim 6 further comprising a second heat exchanger (5), the shell side outlet of the first heat exchanger (2) being in communication with the CO after passing through the second heat exchanger (5)2The inlets of the absorption units (1) are connected.
8. A cryogenic cycle power generation system according to claim 7, wherein the internal heat exchange medium of the second heat exchanger (5) is cooling water.
9. The cryogenic cycle power generation system of claim 7, wherein the CO is2A pressure reducing valve (8) is arranged on a connecting pipeline between the liquid outlet of the desorption unit (4) and the first heat exchanger (2).
10. The cryogenic cycle power generation system of claim 1, further comprising a second heat exchanger (5) and a pressure reducing valve (8), and the first heat exchanger (2) is a shell and tube heat exchanger;
the CO is2An outlet of the absorption unit (1) is connected with a tube-side inlet of the first heat exchanger (2), and a tube-side outlet of the first heat exchanger (2) is connected with an inlet of the circulating booster pump (3);
the CO is2A liquid outlet of the desorption unit (4) is connected with a shell side inlet of the heat exchanger (2) after passing through the pressure reducing valve (8), and the first heat exchangerThe shell pass outlet of the heater (2) and the CO2The inlets of the absorption units (1) are connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122766995.0U CN216240842U (en) | 2021-11-12 | 2021-11-12 | Low-temperature circulating power generation system using carbon dioxide gas as working medium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122766995.0U CN216240842U (en) | 2021-11-12 | 2021-11-12 | Low-temperature circulating power generation system using carbon dioxide gas as working medium |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216240842U true CN216240842U (en) | 2022-04-08 |
Family
ID=80996507
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122766995.0U Active CN216240842U (en) | 2021-11-12 | 2021-11-12 | Low-temperature circulating power generation system using carbon dioxide gas as working medium |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216240842U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113882921A (en) * | 2021-11-12 | 2022-01-04 | 中国石油大学(北京) | Low-temperature circulating power generation system and method using carbon dioxide gas as working medium |
-
2021
- 2021-11-12 CN CN202122766995.0U patent/CN216240842U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113882921A (en) * | 2021-11-12 | 2022-01-04 | 中国石油大学(北京) | Low-temperature circulating power generation system and method using carbon dioxide gas as working medium |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103806969B (en) | System for cycling power generation by means of supercritical CO2 working medium | |
| CN110344898B (en) | Absorption type sea water desalination and closed cycle power generation system | |
| CN104806311B (en) | Amino thermochemical energy-storage system | |
| CN109519243B (en) | Supercritical CO2 and ammonia water combined cycle system and power generation system | |
| CN113339090B (en) | Brayton-organic Rankine cycle type energy storage and power supply method and device | |
| CN112554983A (en) | Liquid carbon dioxide energy storage system and method coupled with kalina cycle | |
| CN201209525Y (en) | Thermo-electric generation apparatus | |
| CN112267920A (en) | Closed supercritical carbon dioxide power generation system and method with carbon capture and utilization and fuel gas circulating waste heat utilization | |
| CN216240842U (en) | Low-temperature circulating power generation system using carbon dioxide gas as working medium | |
| WO2023083242A1 (en) | Low-temperature cyclic power generation system and method with carbon dioxide gas as working medium | |
| CN113540504B (en) | Heat pump-hydrogen energy composite energy storage power generation method and device | |
| CN210317415U (en) | Absorption type seawater desalination and closed cycle power generation system | |
| CN211737228U (en) | Supercritical carbon dioxide combined cycle power generation system with solar energy and geothermal energy coupled | |
| CN111306835B (en) | Ammonia water working medium combined cooling heating and power system utilizing medium-low temperature heat source and working method thereof | |
| CN110541737A (en) | medium-low temperature waste heat power generation system utilizing LNG cold energy and working method thereof | |
| CN213478412U (en) | Liquid oxygen cold energy power generation system | |
| CN111023619B (en) | Green heat pump refrigerating and heating device and method | |
| CN203717054U (en) | Supercritical CO2 working medium circulation power generation system | |
| CN113653548B (en) | Multi-circulation coupling combined supply system with chemical quality improvement and heat storage functions | |
| CN115013094B (en) | Medium-low temperature heat source recovery power circulation system with direct expansion and circulation method | |
| CN114837762B (en) | S-CO 2 Coupled steam Rankine cycle power generation system and working method | |
| CN220036745U (en) | Power generation system utilizing waste heat of ammonia loop of ammonia synthesis device | |
| CN218669484U (en) | Non-afterburning type compressed air energy storage system coupled with organic Rankine cycle system | |
| CN202560490U (en) | Solar power generation system based on heat exchange method | |
| CN114017942B (en) | Solar supercritical carbon dioxide combined cooling, heating and power system and working method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |