CN212029921U - Double-temperature-zone multistage supercooling CO2 refrigeration system - Google Patents
Double-temperature-zone multistage supercooling CO2 refrigeration system Download PDFInfo
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- CN212029921U CN212029921U CN202020143279.XU CN202020143279U CN212029921U CN 212029921 U CN212029921 U CN 212029921U CN 202020143279 U CN202020143279 U CN 202020143279U CN 212029921 U CN212029921 U CN 212029921U
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Abstract
The utility model discloses a multistage super-cooling CO of dual temperature zone2A refrigeration system. Dual-temperature-zone multistage super-cooling CO2The intermediate temperature stage evaporators (i.e. the refrigerating chambers) of the refrigerating system are sequentially communicated with CO2The high-pressure compressor, the high-pressure ejector, the gas cooler, the throttle valve, the primary cooling evaporator and the secondary cooling evaporator are used for completing circulation through the medium-pressure ejector; low temperature grade evaporator (i.e. freezing chamber)) Sequentially connecting a low-pressure level ejector, a four-stage cooling evaporator, a medium-low pressure level ejector, a three-stage cooling evaporator and final CO2Is sucked by the low-pressure stage compressor. The utility model creates the multistage super-cooling CO of dual temperature zone2Refrigerating system for CO2And the cascade multistage supercooling is carried out, so that the irreversible loss in the refrigeration process is obviously reduced, the suction pressure of a compressor is improved, the energy efficiency of a system is obviously improved, and the economic benefit is improved.
Description
Technical Field
The utility model belongs to the technical field of the refrigeration, especially, relate to a multistage super-cooling CO of dual temperature zone2A refrigeration system and applications.
Background
Nowadays, energy and environmental problems are increasingly highlighted. For the refrigeration field, the conventional refrigerant will be gradually reduced due to its higher GWP, which causes the greenhouse effect, and therefore, there is a need to find an alternative refrigerant having excellent performance. Natural working medium CO2Has received widespread attention due to its non-toxic, non-flammable nature.
The refrigerating and freezing requirements in the field of commercial refrigeration and super refrigeration are great, the refrigerating and freezing requirements can be met through a refrigerating device with two temperature zones, however, the conventional CO is2When the double-temperature-zone refrigerating system is used in hot and warm climates, CO is not used before throttling2The fluid temperature is too high, which causes large throttling loss and low efficiency, and limits the popularization and application of the fluid in hot and warm climates.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a multistage super-cooling CO of dual temperature district2The refrigerating system utilizes the components such as an ejector, a subcooler and the like to reduce CO before throttling in a stepped manner2The fluid temperature improves the system efficiency and meets the requirements of simultaneous freezing and refrigeration of the super refrigeration system.
In order to achieve the above purpose, the technical scheme of the utility model is realized as follows:
dual temperature zone multistage super-cooling CO2The refrigerating system mainly comprises a high-pressure stage compressor, a low-pressure stage compressor, a high-pressure stage ejector, a medium-low pressure stage ejector, a low-pressure stage ejector, a first-stage cooling evaporator and a second-stage coolingThe system comprises an evaporator, a three-stage cooling evaporator, a four-stage cooling evaporator, a medium-temperature-stage evaporator, a low-temperature-stage evaporator and a gas cooler.
The outlet of the low-pressure stage compressor is connected with the main flow inlet of the high-pressure stage ejector; the secondary inflow port of the high-pressure ejector is connected with the refrigerant side outlet of the primary cooling evaporator; the outlet of the high-pressure ejector is connected with the inlet of the gas cooler; the outlet of the gas cooler is respectively connected with the inlet of the first throttling valve, the heat medium side inlet of the first-stage cooling evaporator and the main flow inlet of the middle-low pressure stage ejector; the first-stage cooling evaporator heat medium side outlet is respectively connected with the second-stage cooling evaporator heat medium side inlet and the second throttle valve; the second throttle valve is connected with a refrigerant side inlet of the secondary cooling evaporator; the refrigerant side outlet of the secondary cooling evaporator is connected with the main flow inlet of the medium-pressure ejector; the outlet at the heat medium side of the secondary cooling evaporator is respectively connected with the tertiary cooling evaporator and the inlet of the third throttle valve; the outlet of the third throttle valve is connected with the inlet of the intermediate-temperature-stage evaporator; the outlet of the medium-temperature-stage evaporator is connected with the secondary inflow port of the medium-temperature-stage ejector; the outlet of the medium-temperature-stage ejector is connected with the high-pressure-stage compressor;
the heat medium side outlet of the third-stage cooling evaporator is respectively connected with the main flow inlet of the low-pressure ejector and the heat medium side inlet of the fourth-stage cooling evaporator; a heat medium side outlet of the four-stage cooling evaporator is connected with a fourth throttling valve inlet; the outlet of the fourth throttling valve is connected with the inlet of the low-temperature-stage evaporator; the outlet of the low-temperature evaporator is connected with the secondary inflow port of the low-pressure ejector; the outlet of the low-pressure ejector is connected with the refrigerant side inlet of the four-stage cooling evaporator; the refrigerant side outlet of the cooling evaporator is connected with the secondary inflow port of the medium-low pressure ejector; the outlet of the medium-low pressure level ejector is connected with the refrigerant side inlet of the three-level cooling evaporator; the refrigerant side outlet of the three-stage cooling evaporator is connected with the low-pressure stage compressor; the low-pressure stage compressor is connected with the high-pressure stage compressor.
Further, the CO is2Low temperature stage evaporator, CO2The intermediate temperature grade evaporator and each grade of cooling evaporator respectively adopt a finned tube heat exchanger, a finned tube heat exchanger and a sleeve type heat exchangerA heat exchanger or plate heat exchanger; the CO is2The gas cooler is a finned tube heat exchanger.
Further, the gas cooler, CO2Intermediate temperature stage evaporator, CO2The working temperature ranges of the low-temperature stage evaporator, the first-stage cooling evaporator heat medium side, the second-stage cooling evaporator heat medium side, the third-stage cooling evaporator heat medium side, the fourth-stage cooling evaporator heat medium side, the first-stage cooling evaporator refrigerant side, the second-stage cooling evaporator refrigerant side, the third-stage cooling evaporator refrigerant side and the fourth-stage cooling evaporator refrigerant side are respectively 15-140 ℃, 15-10 ℃, 50-20 ℃, 10-30 ℃, 5-20 ℃, 15-10 ℃, 30-0 ℃, 5-25 ℃, 10-15 ℃, 20-15 ℃ and 35-5 ℃. CO22The exhaust pressure range of the high-pressure stage compressor is 7.5-14 MPa; CO22The exhaust pressure range of the low-pressure stage compressor is 1.97-3.97 MPa.
Further, the medium-temperature-stage evaporator is placed in a refrigerating chamber; the low-temperature evaporator is placed in the freezing chamber so as to meet the requirements of different temperature zones. The refrigeration temperature is slightly higher, and dairy products, vegetables, fruits, eggs and the like can be stored; the frozen food can be used for storing meat, fish, etc.
Compared with the prior art, the utility model has the advantages and positive effects that:
(1) two temperature zones CO2The refrigerant of the refrigerating system is only natural working medium CO2. ODP is 0, GWP is 1, the catalyst can not be decomposed at high temperature, and the catalyst is safe, non-toxic, environment-friendly, capable of greatly relieving greenhouse effect and obvious in environmental protection advantage.
(2)CO2The fluid is subjected to continuous two-time cascade supercooling before throttling and entering the medium-temperature evaporator and the low-temperature evaporator, so that the irreversible heat exchange loss in the freezing and refrigerating throttling process can be greatly reduced, and the refrigerating capacity of freezing and refrigerating application is increased.
(3) The high-pressure ejector is arranged to reduce CO entering the gas cooler2The pressure of the fluid is higher, the system operation is safer, the design pressure of the gas cooler is greatly reduced, the manufacturing cost of the gas cooler is reduced, and the weight of the equipment is reduced.
(4) The middle-pressure level ejector is arranged, saturated steam at the outlet of the middle-temperature level evaporator is ejected by high-pressure fluid to form middle pressure slightly higher than the pressure of the middle-temperature level evaporator, the gas-liquid two-phase fluid under the pressure is throttled and reduced in pressure without using a throttle valve, the ejector is used for obtaining the middle pressure, and throttling loss is reduced.
(5) The middle-low pressure level ejector is arranged, high-pressure fluid from the gas cooler is used for ejecting super-cooled steam at the refrigerant side outlet of the four-level cooling evaporator to form intermediate pressure slightly higher than the pressure of the four-level cooling evaporator, throttling and pressure reduction are not carried out on the pressure through a throttling valve in a traditional mode, the ejector is used for obtaining the intermediate pressure, expansion work is recovered, throttling loss is reduced, the suction pressure of a low-pressure level compressor is improved, the compression ratio is reduced, and the system efficiency is improved.
(6) The low-pressure ejector is arranged, saturated steam at the outlet of the low-temperature evaporator is ejected by high-pressure fluid to form intermediate pressure slightly higher than the pressure of the low-temperature evaporator, the gas-liquid two-phase fluid under the pressure is not throttled and depressurized by the throttle valve, the ejector is used for obtaining the intermediate pressure, expansion work is recovered, and throttling loss is reduced.
(7) The system is provided with CO2The high-pressure compressor and the low-pressure compressor have small pressure ratio, are suitable for freezing and refrigerating at lower temperature, can be applied to superstores, cold storages and supermarkets with lower requirements on freezing and refrigerating temperature, and can also be applied to the application fields of slaughterhouses, food processing plants and the like which need freezing and refrigerating at the same time.
Drawings
FIG. 1 shows the utility model of two-temperature zone multi-stage super-cooling CO2A simple schematic of a refrigeration system;
FIG. 2 shows two-temperature zone multi-stage super-cooling CO2And the temperature entropy T-s diagram of the refrigerating system.
Detailed Description
For further understanding of the contents, features and functions of the present invention, the following embodiments are mentioned in detail with reference to the accompanying drawings:
as shown in FIG. 1, a dual temperature zoneStage super-cooled CO2Refrigeration system comprising CO2A medium-temperature stage evaporator and a low-temperature stage evaporator; the intermediate temperature stage evaporator (i.e. the refrigerating chamber) is communicated with CO in sequence2The high-pressure compressor, the high-pressure ejector, the gas cooler, the throttle valve, the primary cooling evaporator and the secondary cooling evaporator are used for completing circulation through the medium-pressure ejector; the low-temperature evaporator (i.e. the freezing chamber) is sequentially connected with the low-pressure ejector, the four-stage cooling evaporator, the medium-low pressure ejector, the three-stage cooling evaporator and the final CO2Is sucked by the low-pressure stage compressor.
Specifically, the working process is as follows:
the first step is as follows: the high-pressure stage compressor 1 compresses CO which is injected by the medium-pressure stage ejector 10 and compressed and mixed with the low-pressure stage compressor 172After passing through a section of pipeline (state a2 in fig. 2), the gas enters the high-pressure ejector 2 (state A3 in fig. 2), and the ejected gas then enters the gas cooler 3 (state a4 in fig. 2).
The second step is that: cooled CO2Dividing into three paths: one path is depressurized through the first throttle valve 4 (as shown in state A20 of FIG. 2), then undergoes evaporative heat absorption in the primary cooler 5 to become a saturated gas state (as shown in state A21 of FIG. 2), and then enters the high-pressure stage ejector 2; the other path of the gas enters the medium-low pressure level ejector 11 as a primary flow, as shown in a state A16 in FIG. 2; the third path is respectively connected with a second throttle valve 6 and a secondary cooling evaporator through a primary cooling evaporator 5 (as shown in a state A5 in figure 2).
The third step: CO throttled by the second throttle 62(state a22 in fig. 2) enters the secondary cooling evaporator 7 to be evaporated and absorbed to become saturated gas (state a13 in fig. 2), and enters the intermediate-pressure ejector 10 as a primary flow; and CO flowing out of the heat medium side of the secondary cooling evaporator 72(as shown in a state A6 of FIG. 2) is divided into two parts, one part enters the third throttle valve 8 for throttling, then is evaporated and absorbed heat in the intermediate-temperature-stage evaporator 9 (as shown in a state A11 of FIG. 2) to become saturated gas (as shown in a state A12 of FIG. 2), the saturated gas A12 is injected by the primary flow A13 in the intermediate-pressure-stage injector 10 as a secondary flow, and the saturated gas A13 and the secondary flow are mixed to a state A14 of FIG. 2 and are finally sucked by the high-pressure-stage compressor 1 to complete the circulation of the refrigerating chamber.
The fourth step: another part of CO flowing out from the heat medium side of the secondary cooling evaporator 72Cooling the heat medium side of the three-stage cooling evaporator 12 (as shown in state a7 in fig. 2), and then dividing the heat medium side into two paths, wherein one path enters the main flow inlet of the low-pressure stage ejector 13 as a primary flow; one path enters the four-stage condenser evaporator 14 for heat medium side evaporative cooling (as shown in state A8 in FIG. 2), then enters the fourth throttle valve 15 for throttling and pressure reduction (as shown in state A9 in FIG. 2), and then enters the low-temperature stage evaporator 16 for evaporation and heat absorption into a saturated gas state to state A10 in FIG. 2.
The fifth step: CO from the three stage cooled evaporator 12 and the low temperature stage evaporator 162The gas is stored in the low-pressure ejector 13, the secondary flow A10 is ejected by the primary flow A7, the two flows are mixed to the state A15 in the figure 2, and lower-pressure CO is formed2. The outlet of the low-pressure ejector 13 is connected with the refrigerant side of a four-stage cooling evaporator 14, and CO is2The evaporation endotherm becomes a saturated gas (state a16 in fig. 2).
And a sixth step: low temperature low pressure CO2Saturated gas A16 enters the ejector 11 as secondary flow and enters the ejector with medium-low pressure level and is simultaneously mixed with one path of CO from the gas cooler 32Merging, injecting the secondary flow A16 by the primary flow A4, and spraying the medium-low pressure medium-low temperature gas-liquid two-phase CO2(as in state a17 of fig. 2).
The seventh step: medium and low pressure and temperature CO2The refrigerant side of the three-stage cooling evaporator 12 evaporates and absorbs heat to become a saturated gas (see state a1 in fig. 2). CO at this time2Is sucked by the low-pressure stage compressor 17 (as in state a18 of fig. 2), and is finally sucked by the high-pressure stage compressor 1 (as in state a19 of fig. 2), completing the refrigeration cycle.
The utility model creates the multistage super-cooling CO of dual temperature zone2In the refrigeration system, when in use, one preferable process condition is as follows: CO22The evaporation temperature of the low-temperature stage evaporator 16 is-35 ℃, the temperature of the medium-temperature stage evaporator 9 is-5 ℃, the temperature of the first-stage cooling evaporator 5 is 25 ℃, and the temperature of the second-stage cooling evaporator 7 is 15 ℃; the temperature of the tertiary cooling evaporator 12 is 5 ℃; the temperature of the four-stage cooling evaporator 14 is-5 ℃; CO22The suction pressure of the high-pressure stage compressor 1 is 3.5MPa, and the exhaust pressure is 10 MPa; CO22The suction pressure of the low-pressure stage compressor 17 is2.5MPa；CO2The secondary flow of the high-pressure ejector 2 has the air suction temperature of 14.2 ℃, the pressure of 5MPa, the main flow temperature of 110 ℃, the pressure of 10MPa and the ejector outlet pressure of 8 MPa. CO22The secondary flow of the medium-pressure ejector 10 has the air suction temperature of-5 ℃, the pressure of 3.05MPa, the main flow temperature of 5.3 ℃, the pressure of 4MPa and the ejector outlet pressure of 3.5 MPa. CO22The secondary flow of the medium-low pressure level ejector 13 has the air suction temperature of minus 19 ℃, the pressure of 2MPa, the main flow temperature of 35 ℃, the pressure of 8MPa and the ejector outlet pressure of 2.5 MPa. CO22The secondary flow of the low-pressure ejector 16 has the air suction temperature of-35 ℃, the pressure of 1.2MPa, the main flow temperature of 5 ℃, the pressure of 3.05MPa and the ejector outlet pressure of 1.2 MPa.
The specific working process is as follows: compressed natural high-temperature high-pressure working medium CO2(10MPa, 110 ℃) enters an ejector device and then CO is ejected out2(8MPa, 35 ℃) and is cooled to 25 ℃ by a gas cooler 3; compressed CO2(8MPa,25 ℃) is divided into three paths: one path is throttled and reduced to 5MPa by a first throttle valve 4, and then is evaporated and absorbed heat to 14.2 ℃ in a refrigerant side of a primary cooler 5, wherein CO is generated at the moment2(5MPa, 14.2 ℃) as secondary flow to enter the high-pressure ejector 2 to complete circulation; another path is to CO2(8MPa,25 ℃) as a primary flow to a medium-low pressure ejector 11; the third path is respectively connected with a second throttling valve 6 and a second cooling evaporator 7 through a first-stage cooling evaporator 5. CO after 6 throttling2(4MPa,25 ℃) enters a refrigerant side 7 of a secondary cooling evaporator to carry out secondary evaporation and heat absorption, and the temperature is reduced to 5.3 ℃ to be used as CO at medium pressure and medium temperature2(4MPa, 5.3 ℃) enters a medium-pressure level ejector 10; and CO flowing out of the heat medium side of the secondary cooling evaporator 72A part of (8MPa,15 ℃) enters a third throttle valve 8 to throttle and reduce the pressure of CO to 3.05MPa2Enters a medium temperature grade evaporator 9 to evaporate and absorb heat to-5 ℃, and CO is absorbed at the moment2Injecting the secondary fluid (3.05MPa and-5 ℃) in the medium-temperature ejector 10; CO of which the pressure is 3.5MPa after injection2Fluid is drawn into the high pressure stage compressor 1, completing the cycle.
Another part of CO flowing out from the heat medium side of the secondary cooling evaporator 72(3.05MPa,15 ℃) into IIIThe heat medium side of the stage cooling evaporator 12 is cooled to 5 ℃, and then the heat medium side is divided into two paths, wherein one path enters the low-pressure stage ejector 13 as a primary flow; one path of the CO enters a14 heat medium side of a four-stage condensation evaporator to be cooled to minus 5 ℃, then enters a fourth throttle valve 15 to be throttled and decompressed to 1.2MPa, enters a low-temperature stage evaporator 16 to be cooled to minus 35 ℃, and at the moment, the CO is cooled2(1.2MPa, -35 ℃) as a secondary stream into the low pressure stage eductor 13 to produce 2MPa of low pressure CO2A gas. The low-pressure ejector 13 is connected with the refrigerant side of the four-stage cooling evaporator 14 for cooling CO2To-19 ℃. CO22(2MPa and 19 ℃) as secondary flow low-pressure gas enters the ejector 11 with medium and low pressure level to generate CO22.5 MPa; then evaporating and absorbing heat to-12 ℃ CO at the refrigerant side of the three-stage cooling evaporator 122A gas. CO22(2.5 MPa-12 ℃) enters a low-pressure stage compressor 17, and is finally sucked into a high-pressure stage compressor 1 to complete the circulation.
As an alternative embodiment of the invention, a particularly preferred embodiment is that the CO is introduced into the reactor2Low temperature stage evaporator, CO2The intermediate temperature grade evaporator and each grade of cooling evaporator respectively adopt a finned tube heat exchanger, a sleeve type heat exchanger or a plate type heat exchanger; the CO is2The gas cooler is a finned tube heat exchanger.
As an optional implementation of the present invention, the dual temperature region CO2The circulating heat exchange fluid being CO2。
The above description is only for the preferred embodiment of the present invention, and should not be taken as limiting the invention, and any modifications, equivalent replacements, improvements, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (4)
1. Dual-temperature-zone multistage super-cooling CO2The refrigeration system is characterized by comprising a high-pressure stage compressor, a low-pressure stage compressor, a high-pressure stage ejector, a medium-low pressure stage ejector, a low-pressure stage ejector, a first-stage cooling evaporator, a second-stage cooling evaporator, a third-stage cooling evaporator and a fourth-stage cooling evaporatorThe system comprises a generator, a medium-temperature-stage evaporator, a low-temperature-stage evaporator and a gas cooler;
the outlet of the high-pressure stage compressor (1) is connected with the main flow inlet of the high-pressure stage ejector (2); the secondary inflow port of the high-pressure ejector (2) is connected with the refrigerant side outlet of the primary cooling evaporator (5); the outlet of the high-pressure ejector (2) is connected with the inlet of the gas cooler (3); the outlet of the gas cooler (3) is respectively connected with the inlet of the first throttle valve (4), the heat medium side inlet of the first-stage cooling evaporator (5) and the main flow inlet of the medium-low pressure stage ejector (11); the outlet of the heat medium side of the primary cooling evaporator (5) is respectively connected with the inlet of the heat medium side of the secondary cooling evaporator (7) and the second throttle valve (6); the second throttle valve (6) is connected with a refrigerant side inlet of the secondary cooling evaporator (7); a refrigerant side outlet of the secondary cooling evaporator (7) is connected with a main flow inlet of the medium-pressure ejector (10); a heat medium side outlet of the secondary cooling evaporator is respectively connected with a heat medium side inlet of the tertiary cooling evaporator (12) and an inlet of the third throttle valve (8); the outlet of the third throttle valve (8) is connected with the inlet of the medium-temperature-stage evaporator (9); the outlet of the medium-temperature-stage evaporator (9) is connected with a secondary inflow port of the medium-pressure-stage ejector (10); the outlet of the medium-pressure ejector (10) is connected with the high-pressure compressor (1);
the outlet of the heat medium side of the three-stage cooling evaporator (12) is respectively connected with the main flow inlet of the low-pressure ejector (13) and the heat medium side inlet of the four-stage cooling evaporator (14); the outlet of the heat medium side of the four-stage cooling evaporator (14) is connected with the inlet of a fourth throttling valve (15); the outlet of the fourth throttling valve (15) is connected with the inlet of the low-temperature-stage evaporator (16); the outlet of the low-temperature evaporator (16) is connected with the secondary inflow port of the low-pressure ejector (13); the outlet of the low-pressure ejector (13) is connected with the refrigerant side inlet of the four-stage cooling evaporator (14); the refrigerant side outlet of the cooling evaporator (14) is connected with the secondary inflow port of the medium-low pressure ejector (11); the outlet of the medium-low pressure level ejector (11) is connected with the refrigerant side inlet of the three-level cooling evaporator (12); the refrigerant side outlet of the three-stage cooling evaporator (12) is connected with a low-pressure stage compressor (17); the low-pressure stage compressor (17) is connected with the high-pressure stage compressor (1).
2. The dual temperature zone multi-stage subcooling CO according to claim 12A refrigeration system, characterized by: the gas cooler (3), the medium-temperature-stage evaporator (9) and the low-temperature-stage evaporator (16) are all fin tube heat exchangers.
3. The dual temperature zone multi-stage subcooling CO according to claim 12A refrigeration system, characterized by: the primary cooling evaporator (5), the secondary cooling evaporator (7), the tertiary cooling evaporator (12) and the quaternary cooling evaporator (14) all adopt sleeve type heat exchangers or plate type heat exchangers.
4. The dual temperature zone multi-stage subcooling CO according to claim 12A refrigeration system, characterized by: transcritical CO2The heat exchange fluid circulated in the two temperature zones is CO2(ii) a CO discharged from high pressure compressor2The pressure range is 7.5 MPa-14 MPa; CO discharge from low pressure stage compressor2The pressure range is 1.97 MPa-3.97 MPa; the working temperature ranges of the gas cooler (3), the medium-temperature grade evaporator (9) and the low-temperature grade evaporator (16) are respectively 15-140 ℃, 15-10 ℃ and 50-20 ℃; the working temperature ranges of the heat medium side of the first-stage cooling evaporator (5), the second-stage cooling evaporator (7), the third-stage cooling evaporator (12) and the fourth-stage cooling evaporator (14) are respectively 10-30 ℃, -5-20 ℃, -15-10 ℃, -30-0 ℃; the working temperature ranges of the refrigerant side of the first-stage cooling evaporator (5), the second-stage cooling evaporator (7), the third-stage cooling evaporator (12) and the fourth-stage cooling evaporator (14) are respectively 5-25 ℃, 10-15 ℃, 20-15 ℃ and 35-5 ℃.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111141055A (en) * | 2020-01-21 | 2020-05-12 | 天津商业大学 | Dual-temperature-zone multistage super-cooling CO2Refrigeration system |
| CN112665214A (en) * | 2020-12-28 | 2021-04-16 | 中国长江三峡集团有限公司 | Integrated system based on energy storage type carbon dioxide circulation cold and heat supply and fire-fighting servo and operation method thereof |
| CN113280523A (en) * | 2021-05-31 | 2021-08-20 | 哈尔滨工业大学 | Injection type heat pump circulating device with supercooling and preheating functions |
| CN115235135A (en) * | 2022-07-20 | 2022-10-25 | 北京航空航天大学 | Gas staged cooling liquefaction system based on vortex tube and ejector |
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2020
- 2020-01-21 CN CN202020143279.XU patent/CN212029921U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111141055A (en) * | 2020-01-21 | 2020-05-12 | 天津商业大学 | Dual-temperature-zone multistage super-cooling CO2Refrigeration system |
| CN111141055B (en) * | 2020-01-21 | 2023-11-28 | 天津商业大学 | Double-temperature-zone multistage supercooling CO 2 Refrigerating system |
| CN112665214A (en) * | 2020-12-28 | 2021-04-16 | 中国长江三峡集团有限公司 | Integrated system based on energy storage type carbon dioxide circulation cold and heat supply and fire-fighting servo and operation method thereof |
| CN112665214B (en) * | 2020-12-28 | 2022-03-11 | 中国长江三峡集团有限公司 | Integrated system based on energy storage type carbon dioxide circulation cold and heat supply and fire-fighting servo and operation method thereof |
| CN113280523A (en) * | 2021-05-31 | 2021-08-20 | 哈尔滨工业大学 | Injection type heat pump circulating device with supercooling and preheating functions |
| CN115235135A (en) * | 2022-07-20 | 2022-10-25 | 北京航空航天大学 | Gas staged cooling liquefaction system based on vortex tube and ejector |
| CN115235135B (en) * | 2022-07-20 | 2023-05-23 | 北京航空航天大学 | Gas classification cooling liquefaction system based on vortex tube and injector |
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