CN201864592U - Full-automatic solar seawater desalination device - Google Patents
Full-automatic solar seawater desalination device Download PDFInfo
- Publication number
- CN201864592U CN201864592U CN2010206240754U CN201020624075U CN201864592U CN 201864592 U CN201864592 U CN 201864592U CN 2010206240754 U CN2010206240754 U CN 2010206240754U CN 201020624075 U CN201020624075 U CN 201020624075U CN 201864592 U CN201864592 U CN 201864592U
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- water
- seawater
- solar energy
- distillation
- energy collector
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- Expired - Fee Related
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- 238000010612 desalination reaction Methods 0.000 title abstract description 9
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- 239000012267 brine Substances 0.000 claims abstract description 14
- 238000010248 power generation Methods 0.000 claims abstract description 7
- 238000004821 distillation Methods 0.000 claims description 18
- 238000004140 cleaning Methods 0.000 abstract description 3
- 238000011033 desalting Methods 0.000 abstract description 3
- 238000001914 filtration Methods 0.000 abstract description 3
- 230000003993 interaction Effects 0.000 abstract description 3
- 238000004062 sedimentation Methods 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 4
- 230000005611 electricity Effects 0.000 description 3
- 239000011552 falling film Substances 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000009835 boiling Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005530 etching Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000011068 load Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920005630 polypropylene random copolymer Polymers 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/141—Wind power
-
- 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
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
-
- 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
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
Abstract
The utility model relates to a seawater desalination device, in particular to a miniaturized and integrated full-automatic solar sea water desalination device, which is characterized by comprising a vacuum pipe-type solar thermal collector, a hot water tank, a water pump, a reducing valve, a seawater distiller, a horizontal pipe-type heat exchanger, a seawater channel, a water-ring vacuum pump, a fresh water tank, a strong brine tank, a water inlet mechanism, a sun patrol mechanism, a sedimentation tank and a wind power generation device. The utility model has the advantages of high stability, compact structure, high reliability and small volume, can be dismounted for maintenance and cleaning and can be widely popularized among masses living on islands and small-scale people in coastal areas. The device adopts a multi-layer filtering measure, has low requirement on water quality and can be used for desalting seawater and bitter salty water; forced convection is carried out on air in a seawater desalination room so that the thermal efficiency is greatly improved, and moreover, the seawater desalination room is sealed so as to avoid caloric loss. The utility model has the characteristics of man-machine interaction, full-automatic control, simple structure and small investment, can be used for all kinds of industrial exhaust heat and has very good prospect.
Description
Technical field
The utility model relates to a kind of sea water desalinating plant, has a kind of miniaturization, integrated full automatic solar sea water desalinating plant.
Background technology
As everyone knows, because the land Freshwater resources is in short supply, sea water desaltination more and more has been subjected to the attention of coastal various countries, the world.Method for desalting seawater has distillation method, flash method, and the multiple-effect method, reverse osmosis method, these all need to consume a large amount of electric power and fuel.The common solar seawater desalination system of being reported in the world at present is based on distillation, all reach industrialized level substantially, but there is a lot of shortcomings, comparatively common general employing natural convection, thermo-efficiency is not high, water vapour latent heat is not fully utilized, cause power loss, wherein with the supporting multistage flash evaporation requirement steady load of traditional method for desalting seawater, be difficult to adapt to the unsettled situation of solar source, be merely able to maximize, and the research of directly-heated return-flow type desalination technology seldom, do not see the industrialized report of commercialization so far.In addition, the many regional tap water of China are very short, and mostly the water-deficient area be a little brackish waters water sources again, and the user of fresh water is suitable dispersive in the time of many, and large-scale system also is not suitable for.The most sophisticated on the relevant sun power desalination techniques is the disc type solar energy distillation device, and its advantage is that latent heat is recycled, but has complex structure, deficiency that cost is high.
Summary of the invention
The utility model proposes a kind of miniaturization at the deficiencies in the prior art, the full automatic solar sea water desalinating plant of integrated form.
The utility model can reach by following measure.
A kind of full automatic solar sea water desalinating plant, it is characterized in that comprising the electron tubes type solar energy collector, hot well tank, water pump, reducing valve, the sea water by distillation device, the transverse tube type interchanger, the seawater groove, water-ring vacuum pump, the fresh water jar, the strong brine jar, water intake mechanism, patrol a day mechanism, settling tank and wind power generation plant are formed, electron tubes type solar energy collector water outlet is connected with transverse tube type interchanger water-in in the sea water by distillation device through water pump, another water outlet of electron tubes type solar energy collector is connected through the water-in of reducing valve with the sea water by distillation device, transverse tube type interchanger water outlet is connected with electron tubes type solar energy collector water-in, sea water by distillation device water-in with through water-ring vacuum pump, fresh water jar one tunnel is connected with settling tank with water intake mechanism, another road is connected with the strong brine jar, strong brine jar one tunnel is connected with the sea water by distillation device, another road is connected with the electron tubes type solar energy collector, and wind power generation plant is a water pump, the water-ring vacuum pump power supply.
Electron tubes type solar energy collector in the utility model can be provided with and patrol a day mechanism, to obtain more energy.
The beneficial effects of the utility model are, adopt wind energy to mend electricity, and full-automation overcomes the under-supply situation of cloudy sun power; Adopt horizontal tube falling film evaporation, be not subjected to external interference, good stability, compact construction, the reliability height, volume is little, and dismantled and assembled maintenance and cleaning can extensively be promoted to island population crowd and coastland small-scale crowd; Device adopts the bed filtration measure, and low to water quality requirement, to seawater, brackish water can both be desalinated; The indoor air of sea water desaltination is forced to convection current, has improved thermo-efficiency greatly, and the caloic loss is avoided in sealing; Man-machine interaction, full automatic control, simple in structure, less investment can be utilized various industrial exhaust heats, has good prospect.
Description of drawings.
Fig. 1 is a kind of structural representation of the present utility model.
Embodiment.
Below in conjunction with accompanying drawing the utility model is further described.
A kind of full automatic solar sea water desalinating plant, comprise electron tubes type solar energy collector 1, hot well tank 2, water pump 3, reducing valve 4, sea water by distillation device 5, transverse tube type interchanger 6, seawater groove 7, water-ring vacuum pump 8, fresh water jar 9, strong brine jar 10, water intake mechanism 11, patrol day mechanism 12, settling tank 14 and wind power generation plant 13 are formed, electron tubes type solar energy collector 1 water outlet is connected with transverse tube type interchanger 6 water-ins in the sea water by distillation device 5 through water pump 3, electron tubes type solar energy collector 1 another water outlet is connected through the water-in of reducing valve 4 with sea water by distillation device 5, transverse tube type interchanger 5 water outlets are connected with electron tubes type solar energy collector 1 water-in, sea water by distillation device 5 water-ins with through water-ring vacuum pump 8, fresh water jar 9 one tunnel is connected with settling tank 14 with water intake mechanism 11, another road is connected with strong brine jar 10, strong brine jar 10 one tunnel is connected with sea water by distillation device 5, another road and 1 connection mutually of electron tubes type solar energy collector, wind power generation plant 13 is a water pump 3, water-ring vacuum pump 8 power supplies, patrol 12 power supplies of day mechanism, electron tubes type solar energy collector 1 in the utility model can be provided with and patrol day mechanism 12, to obtain more energy, the structure and the mode of connection of above-mentioned each integral part are same as the prior art, this does not give unnecessary details
Working process of the present utility model is, after carrying out preheating through fresh water jar and strong brine, the seawater of seawater groove enters the electron tubes type solar energy collector, after in heat collector, drawing solar heat, become the top that hot sea water accumulates in water tank, the hot sea water that water temperature is the highest subsequently enters in the sea water evaporator through reducing valve, spray is born falling film evaporation on the transverse tube type interchanger, most of hot sea water is under the effect of water circulating pump in the hot well tank, pipe internal recycle at the transverse tube type interchanger flows, be the evaporation of seawater heat supply, just constantly boiling evaporation, do not evaporate seawater at base of evaporator, enter at last in the strong brine jar, the water vapour that evaporation produces is sucked by water-ring vacuum pump, made it be condensed into water by the cooling of the water ring in it, and together drained in the dense water pot, the water in the dense water pot is because of having absorbed the latent heat of condensation of water vapour, and temperature raises, heat exchanger is set therein, absorbs its waste heat and come pre-hot sea water; Sea water evaporator is kept higher vacuum under the water ring vacuum pump effect, make it explosive evaporatoin under lower temperature, for making strong brine under negative pressure, be discharged in the normal pressure brine tank, adopt the intermittent drainage mode, whole device has only moving equipment vacuum pump and water circulating pump, and energy is supplied with by wind electricity generating system, when the wind foot, wind energy converts in the bag and can store in battery, start when sun power is not enough with micro-chip control, the supply heat, solar energy equipment adopts solar energy sun-seeking mechanism in addition, absorbs sun power in order to maximum efficiency.This device directly enters solar thermal collection system at seawater and the etching problem and the valve tube scale problems that cause, designed the glass tube with vacuum horizontal positioned, nanometer PPR material coating with seawater corrosion resistance, whole seawater desalination system all scribble anti-corrosion, scale-inhibiting coating (chemical scale-inhibiting agent); More and more higher for preventing concentration of seawater in addition, so it is design has water escape valve, regularly intermittent with its discharge.
The beneficial effects of the utility model are, adopt wind energy to mend electricity, and full-automation overcomes the under-supply situation of cloudy solar energy; Adopt horizontal tube falling film evaporation, be not subjected to external interference, good stability, compact conformation, the reliability height, volume is little, and dismantled and assembled maintenance and cleaning can extensively be promoted to island population crowd and coastal area small-scale crowd; Device adopts the multiple filtration measure, and low to water quality requirement, to seawater, bitter can both be desalinated; The indoor air of desalinization is forced to convection current, has greatly improved the thermal efficiency, and the caloic loss is avoided in sealing; Man-machine interaction, Automatic Control, simple in structure, small investment can be utilized various industrial exhaust heats, has good prospect.
Claims (2)
1. full automatic solar sea water desalinating plant, it is characterized in that comprising the electron tubes type solar energy collector, hot well tank, water pump, reducing valve, the sea water by distillation device, the transverse tube type interchanger, the seawater groove, water-ring vacuum pump, the fresh water jar, the strong brine jar, water intake mechanism, patrol a day mechanism, settling tank and wind power generation plant are formed, electron tubes type solar energy collector water outlet is connected with transverse tube type interchanger water-in in the sea water by distillation device through water pump, another water outlet of electron tubes type solar energy collector is connected through the water-in of reducing valve with the sea water by distillation device, transverse tube type interchanger water outlet is connected with electron tubes type solar energy collector water-in, sea water by distillation device water-in with through water-ring vacuum pump, fresh water jar one tunnel is connected with settling tank with water intake mechanism, another road is connected with the strong brine jar, strong brine jar one tunnel is connected with the sea water by distillation device, another road is connected with the electron tubes type solar energy collector, and wind power generation plant is a water pump, the water-ring vacuum pump power supply.
2. a kind of full automatic solar sea water desalinating plant according to claim 1 is characterized in that the electron tubes type solar energy collector can be provided with to patrol a day mechanism.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010206240754U CN201864592U (en) | 2010-11-25 | 2010-11-25 | Full-automatic solar seawater desalination device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010206240754U CN201864592U (en) | 2010-11-25 | 2010-11-25 | Full-automatic solar seawater desalination device |
Publications (1)
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CN201864592U true CN201864592U (en) | 2011-06-15 |
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CN2010206240754U Expired - Fee Related CN201864592U (en) | 2010-11-25 | 2010-11-25 | Full-automatic solar seawater desalination device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102583611A (en) * | 2012-03-14 | 2012-07-18 | 绍兴文理学院 | Horizontal tube falling film evaporation solar seawater desalination device |
CN107188259A (en) * | 2017-07-12 | 2017-09-22 | 东南大学 | Sea water desalinating unit |
CN109354096A (en) * | 2018-12-13 | 2019-02-19 | 福建工程学院 | Fresnel Lenses solar energy carburetor method desalination plant |
-
2010
- 2010-11-25 CN CN2010206240754U patent/CN201864592U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102583611A (en) * | 2012-03-14 | 2012-07-18 | 绍兴文理学院 | Horizontal tube falling film evaporation solar seawater desalination device |
CN107188259A (en) * | 2017-07-12 | 2017-09-22 | 东南大学 | Sea water desalinating unit |
CN109354096A (en) * | 2018-12-13 | 2019-02-19 | 福建工程学院 | Fresnel Lenses solar energy carburetor method desalination plant |
CN109354096B (en) * | 2018-12-13 | 2021-08-03 | 福建工程学院 | Fresnel lens solar carburetor method seawater desalination device |
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GR01 | Patent grant | ||
C14 | Grant of patent or utility model | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110615 Termination date: 20111125 |
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C17 | Cessation of patent right |