CN206278947U - Heat-pump-type efficient cryogenic sea water desalinating unit - Google Patents
Heat-pump-type efficient cryogenic sea water desalinating unit Download PDFInfo
- Publication number
- CN206278947U CN206278947U CN201621233887.XU CN201621233887U CN206278947U CN 206278947 U CN206278947 U CN 206278947U CN 201621233887 U CN201621233887 U CN 201621233887U CN 206278947 U CN206278947 U CN 206278947U
- Authority
- CN
- China
- Prior art keywords
- outlet
- evaporator
- condenser
- refrigerant
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- 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
Abstract
The utility model is related to a kind of heat-pump-type efficient cryogenic sea water desalinating unit, including compressor, condenser, evaporator, expansion valve and vapour liquid separator；The refrigerant outlet of the compressor is connected with the refrigerant inlet of condenser, the refrigerant inlet of the compressor is connected with the refrigerant outlet of evaporator, the refrigerant inlet of the evaporator is connected with the refrigerant outlet of condenser, and the expansion valve is serially connected on the connecting line between the refrigerant outlet of the refrigerant inlet and condenser of stating evaporator；The condenser is provided with seawater inlet and seawer outlet, the evaporator is provided with steam inlet and water outlet, the seawer outlet of the condenser is connected with the cooling water inlet of diesel engine, the coolant outlet of the diesel engine is connected with the entrance of the vapour liquid separator, and the gas outlet of the vapour liquid separator is connected with the steam inlet of evaporator.The apparatus structure is simple, applied widely, desalinization low cost, reliable and practical.
Description
Technical field
The utility model is related to a kind of heat-pump-type efficient cryogenic sea water desalinating unit, belongs to field of sea water desalting technology.
Background technology
Fresh water is mankind's daily life, the valuable source of production, and tellurian fresh water reserves only account for global total Water
2.53%, and therein 68.7% belong to solid glacier, is distributed in high mountain He Nan, the northern polar regions being difficult by, also
A part of fresh water is buried in the very deep place in underground, it is difficult to exploited, therefore, the fresh water that the mankind can actually utilize only is accounted for entirely
0.26% or so of ball total Water.With population sustainable growth and it is industrial develop rapidly, bring serious freshwater resources
How crisis, develop freshwater resources into the significant problem of contemporary mankind's general concern, in the exploitation of freshwater resources, seawater
The effective way that countries in the world solve water problems is had become with brackish water desalination.
Desalinization is that conventional desalination technology is hot method desalinization using the method production fresh water of seawater desalination
Technology, mainly there is multi-effect flashing steam method and low-temperature multiple-effect distillation.Multi-effect flashing steam method is by the seawater by heating, successively in multiple
It is evaporated in the flash chamber that pressure is gradually reduced, steam is condensed and fresh water is obtained；Low-temperature multiple-effect distillation is will be a series of
The horizontal tube sprinkling falling-film evaporator that pressure is gradually reduced is together in series, and is input into evaporator with a certain amount of steam, by many
Secondary evaporation and condensation, so as to obtain being multiple times than the desalination process of the distilled water of quantity of steam.
But either multi-effect flashing steam method or low-temperature multiple-effect distillation, are required for building up large-scale desalinization dress
Put, the device relies primarily on the waste heat of the generations such as steam power plant, steel mill, chemical plant, there is significant limitation in terms of addressing,
And being on a grand scale due to above-mentioned sea water desalinating unit, it is necessary to large batch of production fresh water, so could effectively reduce every
The production cost of ton fresh water, thus this characteristic determines that they can only be adapted to the fixation in the region of large area and use, it is uncomfortable
For it is small-scale in the region of the small areas such as remote isolated island, rural area and ships, movably produce fresh water, the scope of application has
Significant limitation, it is not practical enough.
Utility model content
The utility model will solve technical problem：Overcome the shortcoming of above-mentioned technology, there is provided a kind of simple structure, applicable model
Enclose wide, desalinization low cost, reliable and practical heat-pump-type efficient cryogenic sea water desalinating unit.
In order to solve the above-mentioned technical problem, the utility model proposes technical scheme be：A kind of heat-pump-type efficient cryogenic sea
Water desalination apparatus, including compressor, condenser, evaporator, expansion valve and vapour liquid separator；The refrigerant outlet of the compressor
Connected with the refrigerant inlet of condenser, the refrigerant inlet of the compressor is connected with the refrigerant outlet of evaporator, described
The refrigerant inlet of evaporator is connected with the refrigerant outlet of condenser, and the expansion valve is serially connected in be stated the refrigerant of evaporator and enter
On connecting line between mouth and the refrigerant outlet of condenser；The condenser is provided with seawater inlet and seawer outlet, institute
State evaporator and be provided with steam inlet and water outlet, the seawer outlet of the condenser connects with the cooling water inlet of diesel engine
Logical, the coolant outlet of the diesel engine is connected with the entrance of the vapour liquid separator, the gas outlet of the vapour liquid separator
Connected with the steam inlet of evaporator, the vapour liquid separator is the vapor-liquid separation that can make water that water vapour is evaporated to by 40 degree
Device.
The further improvement of above-mentioned technical proposal is：System is serially connected between the refrigerant outlet and expansion valve of the condenser
Cryogen storage tank.
The further improvement of above-mentioned technical proposal is：It is provided between the brine outlet and concentrated seawater storage tank of the condenser
Concentrated seawater pump.
The further improvement of above-mentioned technical proposal is：It is provided with fresh between the seawater inlet and seawater storage tank of the condenser
Sea water pump.
The beneficial effect that the utility model brings is：
1）Sea water desalinating unit of the present utility model provides the refrigerant gas of HTHP using compressor to condenser,
By the refrigerant heat release in condenser come heating seawater, and cooling duct by diesel engine is further heated, then by sea
Water is sent in vapour liquid separator, the vapour liquid separator when seawater reaches more than 40 degree by evaporate water vapour, it is described
Vapour liquid separator is transferred in evaporator after the water vapour of evaporation is separated by steam (vapor) outlet, and as the heating heat of evaporator
Source, condenses after exothermic condensation and forms pure fresh water discharge.The utility model has been completely free of traditional hot method desalinization skill
Art to the dependence of thermal source, drive electric energy to suit measures to local conditions using wind-powered electricity generation, diesel engine etc., therefore addressing construction have it is very big
Randomness, be everywhere with, except on ships be applicable in addition to, can also be fitted in the residential households on coastal or island
With, it is applied widely, in the present age of scarcity of fresh water resources, commercially with competitiveness higher.In addition, it is necessary to explanation
It is that diesel engine applies very universal on coastal or island, therefore the cooling duct of diesel engine is used for heating seawater have one
Fixed universality.
2）Sea water desalinating unit of the present utility model during the production stable operation of fresh water, only compressor and water pump
A small amount of acting, effectively reduces the power consumption of desalinization, and then reduce desalinization cost；And further, water
Steam condenses after exothermic condensation and forms pure fresh water so that the waste heat in fresh water is returned as the heat source of evaporator
Receive, not only increase the quality of fresh water, and reduce the power consumption of compressor indirectly, so as to avoid energy heat wave
Take, energy utilization rate is high, reduce further the production cost of desalinization.
Brief description of the drawings
The utility model is described in further detail below in conjunction with the accompanying drawings.
Fig. 1 is the structural representation of the utility model embodiment.
Specific embodiment
Embodiment
The heat-pump-type efficient cryogenic sea water desalinating unit of the present embodiment, including compressor 1, condenser 2, evaporator 3, expansion
Valve 4 and vapour liquid separator 5；The refrigerant outlet of compressor 1 is connected with the refrigerant inlet of condenser 2, the refrigerant of compressor 1
Import is connected with the refrigerant outlet of evaporator 3, and the refrigerant inlet of evaporator 3 is connected with the refrigerant outlet of condenser 2, swollen
Swollen valve 4 is serially connected on the connecting line between the refrigerant outlet of the refrigerant inlet of evaporator 2 and condenser 3.
Condenser 2 is provided with seawater inlet and seawer outlet, and evaporator 3 is provided with steam inlet and water outlet, condensation
The seawer outlet of device 2 is connected with the cooling water inlet of diesel engine 6, the coolant outlet of diesel engine 6 and the entrance of vapour liquid separator 5
Connection, the gas outlet of vapour liquid separator 5 is connected with the steam inlet of evaporator 3.Vapour liquid separator is prior art, this implementation
Vapour liquid separator can preferably make water that the vapour liquid separator of water vapour is evaporated to by 40 degree in example.
The present embodiment can also make following improvement：1）Refrigeration is serially connected between the refrigerant outlet and expansion valve 4 of condenser 2
Agent storage tank 7, the liquid outlet of vapour liquid separator 5 is connected with concentrated seawater storage tank 8, the liquid outlet and concentrated seawater of vapour liquid separator 5
Concentrated seawater pump 9 is provided between storage tank 8.
2）The water outlet of evaporator 3 is connected with condensation water storage tank 10, water outlet and the condensation water storage tank 10 of evaporator 3
Between be provided with condensate pump 11.
The utility model is not limited to the concrete technical scheme described in above-described embodiment, in addition to the implementation, this practicality
It is new to have other embodiment.The technical scheme that all use equivalents are formed, is the guarantor of the utility model requirement
Shield scope.
Claims (6)
1. a kind of heat-pump-type efficient cryogenic sea water desalinating unit, it is characterised in that：Including compressor, condenser, evaporator, expansion
Valve and vapour liquid separator；The refrigerant outlet of the compressor is connected with the refrigerant inlet of condenser, the system of the compressor
Cryogen import is connected with the refrigerant outlet of evaporator, and the refrigerant inlet of the evaporator connects with the refrigerant outlet of condenser
Logical, the expansion valve is serially connected on the connecting line between the refrigerant outlet of the refrigerant inlet and condenser of stating evaporator；
The condenser is provided with seawater inlet and seawer outlet, and the evaporator is provided with steam inlet and water outlet, institute
State the seawer outlet of condenser to be connected with the cooling water inlet of diesel engine, the coolant outlet of the diesel engine and the vapour-liquid are divided
Entrance from device is connected, and the gas outlet of the vapour liquid separator is connected with the steam inlet of evaporator, the vapour liquid separator
For that can make water that the vapour liquid separator of water vapour is evaporated to by 40 degree.
2. heat-pump-type efficient cryogenic sea water desalinating unit according to claim 1, it is characterised in that：The system of the condenser
Cryogen is exported and is serially connected with refrigerant storage tank and expansion valve between.
3. heat-pump-type efficient cryogenic sea water desalinating unit according to claim 1, it is characterised in that：Also stored up including concentrated seawater
Tank, the liquid outlet of the vapour liquid separator is connected with concentrated seawater storage tank.
4. heat-pump-type efficient cryogenic sea water desalinating unit according to claim 3, it is characterised in that：The liquid outlet with
Concentrated seawater pump is provided between concentrated seawater storage tank.
5. heat-pump-type efficient cryogenic sea water desalinating unit according to claim 1, it is characterised in that：Also stored up including condensed water
Tank, the water outlet of the evaporator is connected with the condensation water storage tank.
6. heat-pump-type efficient cryogenic sea water desalinating unit according to claim 5, it is characterised in that：The evaporator it is light
Condensate pump is provided between water out and the condensation water storage tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233887.XU CN206278947U (en) | 2016-11-17 | 2016-11-17 | Heat-pump-type efficient cryogenic sea water desalinating unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621233887.XU CN206278947U (en) | 2016-11-17 | 2016-11-17 | Heat-pump-type efficient cryogenic sea water desalinating unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206278947U true CN206278947U (en) | 2017-06-27 |
Family
ID=59083434
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621233887.XU Active CN206278947U (en) | 2016-11-17 | 2016-11-17 | Heat-pump-type efficient cryogenic sea water desalinating unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206278947U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108408805A (en) * | 2018-03-12 | 2018-08-17 | 南京航空航天大学 | Heat pump sea water desalination coproduction electric system and method |
| CN109269149A (en) * | 2018-07-23 | 2019-01-25 | 南京航空航天大学 | Coproduction electric system and method is concentrated in heat pump solution |
| CN112759011A (en) * | 2020-12-31 | 2021-05-07 | 中谷宏(海南)实业有限公司 | Low-temperature evaporation seawater desalination device without vacuum pump |
-
2016
- 2016-11-17 CN CN201621233887.XU patent/CN206278947U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108408805A (en) * | 2018-03-12 | 2018-08-17 | 南京航空航天大学 | Heat pump sea water desalination coproduction electric system and method |
| CN109269149A (en) * | 2018-07-23 | 2019-01-25 | 南京航空航天大学 | Coproduction electric system and method is concentrated in heat pump solution |
| CN112759011A (en) * | 2020-12-31 | 2021-05-07 | 中谷宏(海南)实业有限公司 | Low-temperature evaporation seawater desalination device without vacuum pump |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101948148B (en) | Energy-saving low-temperature multiple-effect seawater desalting device | |
| CN103043735B (en) | Heat pump type small seawater desalting device | |
| CN106745426B (en) | Seawater desalination system and process based on nano-fluid phase-change cold accumulation and solar drive | |
| CN105923676A (en) | Efficient solar seawater desalination and air conditioner refrigeration combined operation method and system thereof | |
| CN102616973A (en) | Method and device for processing high-saline organic wastewater | |
| CN102336448B (en) | Saline treatment system and method | |
| CN101723476B (en) | Seawater desalination device employing solar energy and vapor compressing distillation | |
| CN206278947U (en) | Heat-pump-type efficient cryogenic sea water desalinating unit | |
| CN211595081U (en) | Sea water desalting device by liquid gravity distillation method | |
| CN105621513A (en) | Solar photovoltaic heat pump sea water desalination and heating and refrigeration coupling system | |
| CN102765768A (en) | Device and method for improving sea water desalinization efficiency through heat pump | |
| CN201634527U (en) | Absorption sea water demineralizing device utilizing waste heat of marine nuclear power plant | |
| CN101130442A (en) | Method for desalinating sea water by using seawater source heat pump technology | |
| CN103787434A (en) | Power-water-salt coproduction process for condensing steam turbine generator unit | |
| CN203007081U (en) | Low-temperature multi-effect distillation desalination system | |
| KR20010106805A (en) | Desalination system with Mechanica l Vapor Recompression | |
| CN211570156U (en) | Heat pump seawater desalination device for bilateral utilization of evaporator condenser | |
| CN211644660U (en) | Double-effect two-stage compression heat pump seawater desalination device | |
| CN105439224A (en) | Pressurized steam type capillary drive sea water desalination system | |
| CN202116342U (en) | Industrial exhaust heat low-temperature multiple-effect seawater desalinization system | |
| CN109293119B (en) | Device for desalinating seawater | |
| CN102267733A (en) | Industrial waste heat low-temperature multi-effect seawater desalting system | |
| CN215048809U (en) | System for recovering waste heat in seawater desalination process and heating domestic water | |
| CN201901602U (en) | Energy-saving, low-temperature and multiple-effect sea water desalinating device | |
| CN211644661U (en) | Air heat dissipation cascade heat pump sea water desalination device of economic benefits and social benefits |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220317 Address after: 266041 17th floor, building 28, Qingdao International academician port, 171 Jinshui Road, Licang District, Qingdao, Shandong Patentee after: Qingdao Fengsheng seawater desalination Research Institute Co.,Ltd. Address before: Room 301, unit 2, building 13, Zhonghai phoenix garden, No. 1, Qingliangmen street, Nanjing, Jiangsu 210024 Patentee before: Gu Weidong |