CN111115733A - Ship seawater desalination system based on injection-compression heat pump technology - Google Patents
Ship seawater desalination system based on injection-compression heat pump technology Download PDFInfo
- Publication number
- CN111115733A CN111115733A CN202010053829.3A CN202010053829A CN111115733A CN 111115733 A CN111115733 A CN 111115733A CN 202010053829 A CN202010053829 A CN 202010053829A CN 111115733 A CN111115733 A CN 111115733A
- Authority
- CN
- China
- Prior art keywords
- temperature evaporator
- outlet
- low
- steam
- inlet
- 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.)
- Granted
Links
- 239000013535 sea water Substances 0.000 title claims abstract description 66
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 27
- 238000007906 compression Methods 0.000 title claims abstract description 22
- 238000005516 engineering process Methods 0.000 title claims abstract description 13
- 239000013505 freshwater Substances 0.000 claims abstract description 29
- 239000000498 cooling water Substances 0.000 claims abstract description 17
- 239000003507 refrigerant Substances 0.000 claims description 29
- 238000001704 evaporation Methods 0.000 claims description 12
- 230000008020 evaporation Effects 0.000 claims description 12
- 238000002347 injection Methods 0.000 claims description 7
- 239000007924 injection Substances 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000009835 boiling Methods 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 description 4
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004873 anchoring Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/046—Treatment of water, waste water, or sewage by heating by distillation or evaporation under vacuum produced by a barometric column
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/008—Mobile apparatus and plants, e.g. mounted on a vehicle
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/043—Treatment of partial or bypass streams
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/10—Energy recovery
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The invention discloses a ship seawater desalination system based on an injection-compression heat pump technology, which comprises an injection-compression heat pump system and a seawater desalination system; the injection-compression heat pump system comprises a compressor, a high-temperature evaporator, an expansion valve, a two-phase ejector and an evaporative condenser; the seawater desalination system comprises a high-temperature evaporator, an evaporative condenser, a fresh water pump, a steam ejector, a low-temperature evaporator and an ejector pump. The invention utilizes the high temperature generated by the injection-compression heat pump technology as the heat source of the seawater desalination system and is not influenced by the ship operation condition; the invention adds two steam ejectors and two low-temperature evaporators on the basis of the vacuum boiling type seawater desalination method, so that the steam generated in the high-temperature evaporator is fully utilized, and the water yield can be further improved; the invention utilizes the injection-compression heat pump technology to recover the heat of the low-temperature cooling water for seawater desalination, and can provide auxiliary cooling for the low-temperature cooling water.
Description
Technical Field
The invention belongs to the technical field of seawater desalination, and particularly relates to a ship seawater desalination system based on an injection-compression heat pump technology.
Background
At present, most of marine seawater desalination devices adopt a vacuum boiling type seawater desalination device which is driven by heat of cylinder liner water of a marine main engine. However, the device has low specific heat water yield and cannot be used when a ship is anchored or in port because of the running time of the main engine of the ship.
Disclosure of Invention
In order to solve the problems in the prior art, the invention aims to design a ship seawater desalination system based on an injection-compression heat pump technology, which can improve the unit heat water yield and is not limited by the running time of a main unit.
In order to achieve the purpose, the technical scheme of the invention is as follows: a ship seawater desalination system based on an injection-compression heat pump technology comprises an injection-compression heat pump system and a seawater desalination system;
the injection-compression heat pump system comprises a compressor, a high-temperature evaporator, an expansion valve, a two-phase ejector and an evaporative condenser;
the compressor is respectively connected with the inlet of the high-temperature evaporator a and the outlet of the evaporative condenser a through refrigerant pipelines;
the outlet of the high-temperature evaporator a is connected with the inlet of the high-temperature evaporator b through a refrigerant pipeline;
the outlet of the high-temperature evaporator b is respectively connected with the inlet of an expansion valve and the inlet of a two-phase ejector through refrigerant pipelines;
the outlet of the expansion valve is connected with the evaporative condenser b through a refrigerant pipeline;
the outlets of the two-phase ejectors are respectively connected with the inlets of the evaporative condensers a through refrigerant pipelines; the other inlet of the two-phase ejector is respectively connected with the outlet of the evaporative condenser b through a refrigerant pipeline;
the seawater desalination system comprises a high-temperature evaporator, an evaporative condenser, a fresh water pump, a steam ejector, a low-temperature evaporator and an ejector pump;
the other inlet and outlet of the high-temperature evaporator a are respectively connected with the main seawater system and the jet pump through seawater pipelines, and the third outlet of the high-temperature evaporator a is connected with the steam jet ejector a through a steam pipeline;
the other inlet and outlet of the high-temperature evaporator b are respectively connected with the main seawater system and the jet pump through seawater pipelines, and the third outlet of the high-temperature evaporator b is connected with the steam jet ejector b through a steam pipeline;
the other inlet of the evaporative condenser b is connected with the outlet of the steam ejector b through a steam pipeline, and the other outlet of the evaporative condenser b is connected with a fresh water pump through a fresh water pipeline;
the other inlet of the evaporative condenser a is connected with the outlet of the steam ejector a through a steam pipeline, and the other outlet of the evaporative condenser a is connected with a fresh water pump through a fresh water pipeline;
the fresh water pump is connected with the fresh water cabinet through a fresh water pipeline;
the outlet of the steam ejector b is connected with the evaporative condenser b through a steam pipeline, and the other inlet of the steam ejector b is connected with the low-temperature evaporator b through a steam pipeline;
the outlet of the steam ejector a is connected with the evaporative condenser a through a steam pipeline, and the other inlet of the steam ejector a is connected with the low-temperature evaporator a through a steam pipeline;
the inlet of the low-temperature evaporator b is connected with a main seawater system through a seawater pipeline, and the outlet of the low-temperature evaporator b is connected with an injection pump;
the other outlet of the low-temperature evaporator b is connected with the low-temperature evaporator a through a cooling water pipeline, and the other inlet of the low-temperature evaporator b is connected with a cooling water inlet;
the inlet of the low-temperature evaporator a is connected with a main seawater system through a seawater pipeline, and the outlet of the low-temperature evaporator a is connected with an injection pump;
the other outlet of the low-temperature evaporator a is connected with a cooling water outlet;
the other inlet of the jet pump is connected with the main seawater system through a seawater pipeline, and the outlet of the jet pump is connected to the outboard.
Further, the evaporation temperature range of the high-temperature evaporator a is 60-70 ℃, and the evaporation temperature range of the high-temperature evaporator b is 40-50 ℃; the evaporation temperature range of the low-temperature evaporator a is 15-20 ℃, and the evaporation temperature range of the low-temperature evaporator b is 20-25 ℃.
Compared with the prior art, the invention has the following beneficial effects:
1. the invention utilizes the high temperature generated by the injection-compression heat pump technology as the heat source of the seawater desalination system, is not influenced by the running condition of the ship, and can be used during anchoring, port-leading and maneuvering sailing;
2. the invention adds two steam ejectors and two low-temperature evaporators on the basis of the vacuum boiling type seawater desalination method, so that the steam generated in the high-temperature evaporator is fully utilized, and the water yield can be further improved;
3. the invention utilizes the injection-compression heat pump technology to recover the heat of the low-temperature cooling water for seawater desalination, and can provide auxiliary cooling for the low-temperature cooling water.
Drawings
FIG. 1 is a schematic diagram of the system of the present invention.
In the figure: 1. the system comprises a compressor, 2, high-temperature evaporators a and 3, high-temperature evaporators b and 4, an expansion valve 5, a two-phase ejector 6, evaporative condensers b and 7, evaporative condensers a and 8, a fresh water pump 9, steam ejectors b and 10, steam ejectors a and 11, low-temperature evaporators b and 12, low-temperature evaporators a and 13 and an injection pump.
Detailed Description
The invention is explained in more detail below with reference to the figures and examples. As shown in fig. 1, a marine seawater desalination system based on an injection-compression heat pump technology comprises an injection-compression heat pump system and a seawater desalination system;
the injection-compression heat pump system comprises a compressor 1, a high-temperature evaporator, an expansion valve 4, a two-phase ejector 5 and an evaporative condenser;
the compressor 1 is respectively connected with the inlet of the high-temperature evaporator a2 and the outlet of the evaporative condenser a7 through refrigerant pipelines;
the outlet of the high-temperature evaporator a2 is connected with the inlet of the high-temperature evaporator b3 through a refrigerant pipeline;
the outlet of the high-temperature evaporator b3 is respectively connected with the inlet of an expansion valve 4 and the inlet of a two-phase ejector 5 through refrigerant pipelines;
the outlet of the expansion valve 4 is connected with the evaporative condenser b6 through a refrigerant pipeline;
the outlets of the two-phase ejector 5 are respectively connected with the inlets of the evaporative condensers a7 through refrigerant pipelines; the other inlets of the two-phase ejector 5 are respectively connected with the outlets of the evaporative condensers b6 through refrigerant pipelines;
the seawater desalination system comprises a high-temperature evaporator, an evaporative condenser, a fresh water pump 8, a steam ejector, a low-temperature evaporator and an ejector pump 13;
the other inlet and outlet of the high-temperature evaporator a2 are respectively connected with the main seawater system and the jet pump 13 through seawater pipelines, and the third outlet of the high-temperature evaporator a2 is connected with the steam ejector a10 through a steam pipeline;
the other inlet and outlet of the high-temperature evaporator b3 are respectively connected with the main seawater system and the jet pump 13 through seawater pipelines, and the third outlet of the high-temperature evaporator b3 is connected with the steam ejector b9 through a steam pipeline;
the other inlet of the evaporative condenser b6 is connected with the outlet of the steam ejector b9 through a steam pipeline, and the other outlet of the evaporative condenser b6 is connected with the fresh water pump 8 through a fresh water pipeline;
the other inlet of the evaporative condenser a7 is connected with the outlet of the steam ejector a10 through a steam pipeline, and the other outlet is connected with the fresh water pump 8 through a fresh water pipeline;
the fresh water pump 8 is connected with the fresh water cabinet through a fresh water pipeline;
the outlet of the steam ejector b9 is connected with the evaporative condenser b6 through a steam pipeline, and the other inlet is connected with the low-temperature evaporator b11 through a steam pipeline;
the outlet of the steam ejector a10 is connected with the evaporative condenser a7 through a steam pipeline, and the other inlet is connected with the low-temperature evaporator a12 through a steam pipeline;
the inlet of the low-temperature evaporator b11 is connected with the main seawater system through a seawater pipeline, and the outlet is connected with the jet pump 13;
the other outlet of the low-temperature evaporator b11 is connected with the low-temperature evaporator a12 through a cooling water pipeline, and the other inlet of the low-temperature evaporator b11 is connected with a cooling water inlet;
the inlet of the low-temperature evaporator a12 is connected with the main seawater system through a seawater pipeline, and the outlet is connected with the jet pump 13;
the other outlet of the low-temperature evaporator a12 is connected with a cooling water outlet;
the other inlet of the jet pump 13 is connected with the main seawater system through a seawater pipeline, and the outlet is connected to the outboard.
Furthermore, the evaporation temperature range of the high-temperature evaporator a2 is 60-70 ℃, and the evaporation temperature range of the high-temperature evaporator b3 is 40-50 ℃; the evaporation temperature range of the low-temperature evaporator a12 is 15-20 ℃, and the evaporation temperature range of the low-temperature evaporator b11 is 20-25 ℃.
The working process of the invention is as follows:
when the invention works, in the injection-compression heat pump system, the compressor 1 compresses the refrigerant, the generated high-temperature and high-pressure refrigerant gas enters the high-temperature evaporator a2 and the high-temperature evaporator b3 in sequence for condensation and heat release, and the refrigerant gas is used as a heat source for heating the two high-temperature evaporators. One path of the low-temperature high-pressure refrigerant liquid after condensation and heat release flows into the expansion valve 4 for throttling, the throttled low-temperature low-pressure refrigerant liquid is evaporated and absorbs heat in the evaporative condenser b6, and the high-temperature low-pressure refrigerant gas after heat absorption is injected in the two-phase ejector 5; the other stream flows to the two-phase ejector 5 as the working fluid. The two-phase refrigerant mixed by the working fluid and the ejection fluid enters the evaporative condenser a7 to be evaporated and absorbed to be changed into high-temperature low-pressure refrigerant gas, and then the refrigerant gas is compressed in the compressor 1 to complete the cycle.
In a seawater desalination system, seawater from a main seawater system respectively enters a high-temperature evaporator a2 and a high-temperature evaporator b3, exchanges heat with a refrigerant in a vacuum state and then evaporates to generate steam, respectively enters a steam ejector a10 and a steam ejector b9 as working fluid, drives the two steam ejectors to generate vacuum, and respectively injects the steam in a low-temperature evaporator a12 and a low-temperature evaporator b 11; seawater from a main seawater system enters the low-temperature evaporator a12 and the low-temperature evaporator b13 respectively, is evaporated at a low temperature under a vacuum environment to generate steam, and is injected by the steam injector a10 and the steam injector b9 respectively. The seawater evaporates and absorbs heat to ensure that the temperature range in the two low-temperature evaporators is 10-20 ℃. The steam sprayed by the steam sprayer a10 and the steam sprayer b9 enters the evaporative condenser a7 and the evaporative condenser b6 respectively to exchange heat with the refrigerant and condense, and the generated fresh water enters the fresh water cabinet through the fresh water pump 8.
The seawater from the main seawater system drives the ejector pump 13 and is discharged to the outside, and the ejector pump 13 is evacuated. The ejector pump 13 pumps the remaining high-salt seawater in the high-temperature evaporator a2, the high-temperature evaporator b3, the low-temperature evaporator a12 and the low-temperature evaporator b11, and the air in the evaporative condenser a7 and the evaporative condenser b6 to maintain the vacuum degree of the whole system.
The cooling water from the cooling water system flows through the low-temperature evaporator b11 and the low-temperature evaporator a12 in sequence to exchange heat with the seawater. And cooling the equipment by the cooled low-temperature cooling water in each cooling water equipment.
Although specific embodiments of the present invention have been described above, it will be appreciated by those skilled in the art that these are merely illustrative and that various changes and modifications may be made in the embodiments of the invention without departing from the principles and spirit of the invention.
Claims (2)
1. A ship seawater desalination system based on an injection-compression heat pump technology is characterized in that: comprises an injection-compression heat pump system and a seawater desalination system;
the injection-compression heat pump system comprises a compressor (1), a high-temperature evaporator, an expansion valve (4), a two-phase ejector (5) and an evaporative condenser;
the compressor (1) is respectively connected with an inlet of the high-temperature evaporator a (2) and an outlet of the evaporative condenser a (7) through refrigerant pipelines;
the outlet of the high-temperature evaporator a (2) is connected with the inlet of the high-temperature evaporator b (3) through a refrigerant pipeline;
the outlet of the high-temperature evaporator b (3) is respectively connected with the inlet of an expansion valve (4) and the inlet of a two-phase ejector (5) through a refrigerant pipeline;
the outlet of the expansion valve (4) is connected with the evaporative condenser b (6) through a refrigerant pipeline;
the outlet of the two-phase ejector (5) is respectively connected with the inlet of an evaporative condenser a (7) through a refrigerant pipeline; the other inlet of the two-phase ejector (5) is respectively connected with the outlet of the evaporative condenser b (6) through a refrigerant pipeline;
the seawater desalination system comprises a high-temperature evaporator, an evaporative condenser, a fresh water pump (8), a steam ejector, a low-temperature evaporator and an ejector pump (13);
the other inlet and outlet of the high-temperature evaporator a (2) are respectively connected with a main seawater system and an injection pump (13) through seawater pipelines, and the third outlet of the high-temperature evaporator a (2) is connected with a steam injector a (10) through a steam pipeline;
the other inlet and outlet of the high-temperature evaporator b (3) are respectively connected with a main seawater system and an injection pump (13) through seawater pipelines, and the third outlet of the high-temperature evaporator b (3) is connected with a steam injector b (9) through a steam pipeline;
the other inlet of the evaporative condenser b (6) is connected with the outlet of the steam ejector b (9) through a steam pipeline, and the other outlet of the evaporative condenser b (6) is connected with a fresh water pump (8) through a fresh water pipeline;
the other inlet of the evaporative condenser a (7) is connected with the outlet of the steam ejector a (10) through a steam pipeline, and the other outlet of the evaporative condenser a (7) is connected with a fresh water pump (8) through a fresh water pipeline;
the fresh water pump (8) is connected with the fresh water cabinet through a fresh water pipeline;
the outlet of the steam ejector b (9) is connected with the evaporative condenser b (6) through a steam pipeline, and the other inlet of the steam ejector b (9) is connected with the low-temperature evaporator b (11) through a steam pipeline;
the outlet of the steam ejector a (10) is connected with the evaporative condenser a (7) through a steam pipeline, and the other inlet of the steam ejector a (10) is connected with the low-temperature evaporator a (12) through a steam pipeline;
the inlet of the low-temperature evaporator b (11) is connected with a main seawater system through a seawater pipeline, and the outlet of the low-temperature evaporator b (11) is connected with an injection pump (13);
the other outlet of the low-temperature evaporator b (11) is connected with the low-temperature evaporator a (12) through a cooling water pipeline, and the other inlet of the low-temperature evaporator b is connected with a cooling water inlet;
the inlet of the low-temperature evaporator a (12) is connected with a main seawater system through a seawater pipeline, and the outlet of the low-temperature evaporator a (12) is connected with an injection pump (13);
the other outlet of the low-temperature evaporator a (12) is connected with a cooling water outlet;
the other inlet of the jet pump (13) is connected with the main seawater system through a seawater pipeline, and the outlet of the jet pump is connected to the outboard.
2. The marine seawater desalination system based on the injection-compression heat pump technology as claimed in claim 1, wherein: the evaporation temperature range of the high-temperature evaporator a (2) is 60-70 ℃, and the evaporation temperature range of the high-temperature evaporator b (3) is 40-50 ℃; the evaporation temperature range of the low-temperature evaporator a (12) is 15-20 ℃, and the evaporation temperature range of the low-temperature evaporator b (11) is 20-25 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010053829.3A CN111115733B (en) | 2020-01-17 | 2020-01-17 | Ship sea water desalination system based on injection-compression heat pump technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202010053829.3A CN111115733B (en) | 2020-01-17 | 2020-01-17 | Ship sea water desalination system based on injection-compression heat pump technology |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN111115733A true CN111115733A (en) | 2020-05-08 |
| CN111115733B CN111115733B (en) | 2024-03-29 |
Family
ID=70490101
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202010053829.3A Active CN111115733B (en) | 2020-01-17 | 2020-01-17 | Ship sea water desalination system based on injection-compression heat pump technology |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111115733B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1043551A2 (en) * | 1999-04-06 | 2000-10-11 | Mayekawa Mfg Co.Ltd. | Vapor jet refrigerating and heat pumping apparatus for a ship |
| JP2000356432A (en) * | 1999-04-06 | 2000-12-26 | Mayekawa Mfg Co Ltd | Marine steam jet refrigerating/heat pump apparatus |
| WO2004074187A1 (en) * | 2003-02-21 | 2004-09-02 | Abraham Ebenezer Muthunayagam | A process, system and design for desalination of sea water |
| CN102557168A (en) * | 2011-12-05 | 2012-07-11 | 北京朗新明环保科技有限公司 | Heat-pipe low-temperature multi-effect sea water desalinating system and process flow |
| CN103043736A (en) * | 2013-01-23 | 2013-04-17 | 林贤华 | Heat-pump based all-purpose sea water desalination system |
| KR101683392B1 (en) * | 2015-08-25 | 2016-12-07 | 한국과학기술원 | Ejector type refrigeration and purification system for cooling of refrigerants and purifying of fluids |
| CN107200372A (en) * | 2017-06-22 | 2017-09-26 | 陕西科技大学 | A kind of seawater desalination system and method |
| CN211619985U (en) * | 2020-01-17 | 2020-10-02 | 大连海事大学 | Ship seawater desalination system based on injection-compression heat pump technology |
-
2020
- 2020-01-17 CN CN202010053829.3A patent/CN111115733B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1043551A2 (en) * | 1999-04-06 | 2000-10-11 | Mayekawa Mfg Co.Ltd. | Vapor jet refrigerating and heat pumping apparatus for a ship |
| JP2000356432A (en) * | 1999-04-06 | 2000-12-26 | Mayekawa Mfg Co Ltd | Marine steam jet refrigerating/heat pump apparatus |
| WO2004074187A1 (en) * | 2003-02-21 | 2004-09-02 | Abraham Ebenezer Muthunayagam | A process, system and design for desalination of sea water |
| CN102557168A (en) * | 2011-12-05 | 2012-07-11 | 北京朗新明环保科技有限公司 | Heat-pipe low-temperature multi-effect sea water desalinating system and process flow |
| CN103043736A (en) * | 2013-01-23 | 2013-04-17 | 林贤华 | Heat-pump based all-purpose sea water desalination system |
| KR101683392B1 (en) * | 2015-08-25 | 2016-12-07 | 한국과학기술원 | Ejector type refrigeration and purification system for cooling of refrigerants and purifying of fluids |
| CN107200372A (en) * | 2017-06-22 | 2017-09-26 | 陕西科技大学 | A kind of seawater desalination system and method |
| CN211619985U (en) * | 2020-01-17 | 2020-10-02 | 大连海事大学 | Ship seawater desalination system based on injection-compression heat pump technology |
Also Published As
| Publication number | Publication date |
|---|---|
| CN111115733B (en) | 2024-03-29 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102128508B (en) | Ejector throttling and vapor supplementing system and heat pump or refrigerating system vapor supplementing method | |
| CN110345690B (en) | Double-ejector synergistic refrigeration cycle system for double-temperature refrigerator and working method | |
| CN108106048B (en) | Ejector expansion self-cascade refrigeration cycle system and working process | |
| CN208920650U (en) | A kind of refrigeration system | |
| CN103759449B (en) | The two-stage steam compression type circulatory system of dual jet synergy | |
| CN201666686U (en) | Throttling air supply system with ejectors | |
| CN103954061A (en) | Single-stage vapor compression circulatory system for supercooling synergizing of injector | |
| CN109737639A (en) | The steam compressed mixed refrigeration systems of injection-and its course of work of solar energy auxiliary | |
| CN104019579A (en) | Mixed working medium low-temperature refrigerating cycle system driving ejector through waste heat | |
| CN106524569B (en) | A kind of double ejector refrigeration systems and its method | |
| CN105066508B (en) | A kind of efficient injection absorption refrigerating machine for freezing and refrigeration | |
| CN211619985U (en) | Ship seawater desalination system based on injection-compression heat pump technology | |
| CN108800653A (en) | A kind of mixed working fluid jet refrigeration circulation system of injector throttling synergy | |
| CN112556230B (en) | Ship solar vapor compression refrigeration cycle system with two-stage ejector | |
| CN109737622A (en) | The two-stage Auto-cascade cycle low-temperature refrigeration circulating device and round-robin method of duplex injector synergy | |
| CN110081628A (en) | Trans-critical cycle CO with separator2Mixed working fluid back pressure injecting type combined cooling and power system | |
| CN206160542U (en) | Overlapping formula refrigerating units | |
| CN211619984U (en) | Ship seawater desalination system with auxiliary cooling function | |
| CN111115733A (en) | Ship seawater desalination system based on injection-compression heat pump technology | |
| CN105546870B (en) | Hypergravity Thermal driven chiller and method | |
| CN109307377B (en) | Two-stage self-cascade refrigeration cycle system and circulation method adopting ejector to increase efficiency | |
| CN215638111U (en) | Jet refrigeration system and refrigeration equipment | |
| CN113280524B (en) | Large temperature difference heat exchange system provided with multiple ejectors | |
| CN114251865A (en) | Cold and hot combined supply injection circulation system and working method thereof | |
| CN106403355A (en) | Ejection refrigeration system with double evaporators |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | 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 |