CN105439229A - Sea water desalination treatment system - Google Patents
Sea water desalination treatment system Download PDFInfo
- Publication number
- CN105439229A CN105439229A CN201510892373.9A CN201510892373A CN105439229A CN 105439229 A CN105439229 A CN 105439229A CN 201510892373 A CN201510892373 A CN 201510892373A CN 105439229 A CN105439229 A CN 105439229A
- Authority
- CN
- China
- Prior art keywords
- sea water
- seawater
- runner
- water desalination
- heat exchange
- 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.)
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Classifications
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- 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
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- 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
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- 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
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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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
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- 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)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention relates to a sea water desalination treatment system. The sea water desalination treatment system comprises a plurality of sea water desalination devices. Each sea water desalination device comprises a heat exchange flow channel, a steam channel, porous media and a sea water flow channel. The sea water flow channel is located at the bottom of the sea water desalination device. One end of the sea water flow channel is connected with a sea water inflow pipeline, and the other end of the sea water flow channel is connected with a sea water outflow pipeline. The porous media are located at the position above the sea water flow channel. The heat exchange flow channel is located at the position of the top of the sea water desalination device. The steam channel is located at the position below the heat exchange flow channel. The steam channel is internally provided with a plurality of heat conduction fins. The heat exchange flow channels of the sea water desalination devices are connected through high temperature heat source pipelines. Outlets of the steam channels of the sea water desalination devices are connected with fresh water pipelines. The end of each fresh water pipeline connected with each steam channel is provided with a condenser. The sea water desalination devices are utilized to perform sea water desalination, the sea water desalination efficiency can be improved greatly, the same heat source pipeline can be used for many times, and the production energy is saved.
Description
Technical field
The present invention relates to a kind of desalination treatment system.
Background technology
Namely sea water desaltination utilizes sea water desalinization to produce fresh water.Be the increment technique of increasing income realizing water resources utilization, fresh water total amount can be increased, and not by space-time and weather effect, the stable water supply such as coastal Drinking Water for Residents and Industrial Boiler moisturizing can be ensured.
The process meaning sea water desaltination of fresh water is obtained from seawater.Method for desalting seawater now used has seawater freezing method, electroosmose process, distillation method, reverse osmosis method.But existing sea water desalinating plant often complex structure, operation inconvenience during use.
Summary of the invention
The object of the invention is, in order to overcome above deficiency, to provide a kind of desalination treatment system.
Object of the present invention realizes like this:
A kind of desalination treatment system, wherein, comprise multiple sea water desalinating plant, described sea water desalinating plant comprises heat exchange runner, vapour passage, porous medium and seawater runner, described seawater runner is positioned at bottom described sea water desalinating plant, described seawater runner one end connects seawater inflow line, the other end connects seawater and flows out pipeline, described porous medium is positioned at described seawater runner top position, described heat exchange runner is positioned at described sea water desalinating plant tip position, described vapour passage is positioned at described heat exchange runner lower position, and be positioned at porous medium top position, seawater in described seawater runner is drawn into vapour passage by porous medium, multiple heat-conducting fins is provided with in described vapour passage, the heat exchange runner of described multiple sea water desalinating plant realizes connecting by high temperature heat source pipeline, and the vapour passage outlet of described multiple sea water desalinating plant all connects fresh water pipeline, and the coupling end of described each fresh water pipeline and vapour passage is provided with condenser.
Above-mentioned a kind of desalination treatment system, wherein, described porous medium is capillary wick.
Compared with prior art, beneficial effect of the present invention is:
Adopt multiple sea water desalinating plant to carry out sea water desaltination, can greatly improve sea water desaltination efficiency, and same thermal source pipeline can realize repeatedly utilizing, save and produce the energy.By the heat of thermal source pipeline, the seawater moisture at porous medium top is evaporated, water vapour after evaporation flows out in vapour passage, fresh water is obtained by after the condenser condenses on fresh water pipeline, realize the desalination of seawater, structure simple operations of the present invention is convenient, and the automatization flow process that desalinizes seawater can greatly reduce manually.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Embodiment
Below in conjunction with accompanying drawing, the invention will be further described.
As shown in the figure, a kind of desalination treatment system, wherein, comprise multiple sea water desalinating plant 6, described sea water desalinating plant 6 comprises heat exchange runner 7, vapour passage 9, porous medium 10 and seawater runner 11, described seawater runner 11 is positioned at bottom described sea water desalinating plant 6, described seawater runner 11 one end connects seawater inflow line 3, the other end connects seawater and flows out pipeline 5, described porous medium 10 is positioned at described seawater runner 11 top position, described heat exchange runner 7 is positioned at described sea water desalinating plant 6 tip position, described vapour passage 9 is positioned at described heat exchange runner 7 lower position, and be positioned at porous medium 10 top position, seawater in described seawater runner 11 is drawn into vapour passage 9 by porous medium 10, multiple heat-conducting fins 8 is provided with in described vapour passage 9, the heat exchange runner 7 of described multiple sea water desalinating plant 6 realizes connecting by high temperature heat source pipeline 1, the vapour passage 9 of described multiple sea water desalinating plant 6 exports and all connects fresh water pipeline 4, and described each fresh water pipeline 4 is provided with condenser 2 with the coupling end of vapour passage 9.Described porous medium 10 is capillary wick.
Compared with prior art, beneficial effect of the present invention is:
Adopt multiple sea water desalinating plant to carry out sea water desaltination, can greatly improve sea water desaltination efficiency, and same thermal source pipeline can realize repeatedly utilizing, save and produce the energy.By the heat of thermal source pipeline, the seawater moisture at porous medium top is evaporated, water vapour after evaporation flows out in vapour passage, fresh water is obtained by after the condenser condenses on fresh water pipeline, realize the desalination of seawater, structure simple operations of the present invention is convenient, and the automatization flow process that desalinizes seawater can greatly reduce manually.
Above embodiment is only used to further illustrate the present invention; can not be interpreted as limiting the scope of the invention, some nonessential improvement that those skilled in the art's foregoing according to the present invention is made and adjustment all belong to protection scope of the present invention.
Claims (2)
1. a desalination treatment system, it is characterized in that, comprise multiple sea water desalinating plant, described sea water desalinating plant comprises heat exchange runner, vapour passage, porous medium and seawater runner, described seawater runner is positioned at bottom described sea water desalinating plant, described seawater runner one end connects seawater inflow line, the other end connects seawater and flows out pipeline, described porous medium is positioned at described seawater runner top position, described heat exchange runner is positioned at described sea water desalinating plant tip position, described vapour passage is positioned at described heat exchange runner lower position, and be positioned at porous medium top position, seawater in described seawater runner is drawn into vapour passage by porous medium, multiple heat-conducting fins is provided with in described vapour passage, the heat exchange runner of described multiple sea water desalinating plant realizes connecting by high temperature heat source pipeline, and the vapour passage outlet of described multiple sea water desalinating plant all connects fresh water pipeline, and the coupling end of described each fresh water pipeline and vapour passage is provided with condenser.
2. a kind of desalination treatment system as claimed in claim 1, is characterized in that, described porous medium is capillary wick.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510892373.9A CN105439229A (en) | 2015-12-08 | 2015-12-08 | Sea water desalination treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510892373.9A CN105439229A (en) | 2015-12-08 | 2015-12-08 | Sea water desalination treatment system |
Publications (1)
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CN105439229A true CN105439229A (en) | 2016-03-30 |
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Family Applications (1)
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CN201510892373.9A Pending CN105439229A (en) | 2015-12-08 | 2015-12-08 | Sea water desalination treatment system |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106477658A (en) * | 2016-10-31 | 2017-03-08 | 武汉大学 | A kind of seawater desalination system based on LNG cold energy and method |
CN108622966A (en) * | 2018-06-22 | 2018-10-09 | 南通中船机械制造有限公司 | Integrated economic benefits and social benefits five in one plate type sea water desalinating device and its working method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004283798A (en) * | 2003-03-25 | 2004-10-14 | Masato Kino | Liquid separation apparatus using membrane |
CN103496751A (en) * | 2013-10-23 | 2014-01-08 | 武汉大学 | Low-temperature energy-saving marine seawater desalination system |
CN104445481A (en) * | 2014-12-19 | 2015-03-25 | 武汉大学 | Waste heat electricity-water coproduction system |
-
2015
- 2015-12-08 CN CN201510892373.9A patent/CN105439229A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004283798A (en) * | 2003-03-25 | 2004-10-14 | Masato Kino | Liquid separation apparatus using membrane |
CN103496751A (en) * | 2013-10-23 | 2014-01-08 | 武汉大学 | Low-temperature energy-saving marine seawater desalination system |
CN104445481A (en) * | 2014-12-19 | 2015-03-25 | 武汉大学 | Waste heat electricity-water coproduction system |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106477658A (en) * | 2016-10-31 | 2017-03-08 | 武汉大学 | A kind of seawater desalination system based on LNG cold energy and method |
CN106477658B (en) * | 2016-10-31 | 2019-09-10 | 武汉大学 | A kind of seawater desalination system and method based on LNG cold energy |
CN108622966A (en) * | 2018-06-22 | 2018-10-09 | 南通中船机械制造有限公司 | Integrated economic benefits and social benefits five in one plate type sea water desalinating device and its working method |
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Application publication date: 20160330 |
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