DE19508821A1 - Solar-powered sea water desalination - Google Patents
Solar-powered sea water desalinationInfo
- Publication number
- DE19508821A1 DE19508821A1 DE19508821A DE19508821A DE19508821A1 DE 19508821 A1 DE19508821 A1 DE 19508821A1 DE 19508821 A DE19508821 A DE 19508821A DE 19508821 A DE19508821 A DE 19508821A DE 19508821 A1 DE19508821 A1 DE 19508821A1
- Authority
- DE
- Germany
- Prior art keywords
- container
- membrane
- solution
- sea water
- concentrated
- 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.)
- Withdrawn
Links
- 239000013535 sea water Substances 0.000 title claims abstract description 12
- 238000010612 desalination reaction Methods 0.000 title claims abstract 3
- 239000012528 membrane Substances 0.000 claims abstract description 16
- 239000000243 solution Substances 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 6
- 230000003204 osmotic effect Effects 0.000 claims abstract description 5
- 239000012266 salt solution Substances 0.000 claims abstract description 4
- 239000013505 freshwater Substances 0.000 claims description 2
- IHQKEDIOMGYHEB-UHFFFAOYSA-M sodium dimethylarsinate Chemical class [Na+].C[As](C)([O-])=O IHQKEDIOMGYHEB-UHFFFAOYSA-M 0.000 claims description 2
- 239000012267 brine Substances 0.000 abstract description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract description 2
- 235000009508 confectionery Nutrition 0.000 abstract 1
- 150000003839 salts Chemical class 0.000 description 4
- 238000004821 distillation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
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
- C02F1/14—Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/10—Accessories; Auxiliary operations
-
- 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
- Y02A20/131—Reverse-osmosis
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Nanotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
In zwei Behältern A und B befinden sich je eine halbdurchlässige Membrane die nur E Wasser und kein Salz durchläßt. In den Hohlraum C befindet sich konzentrierte Salzlösung mit einen Salzgehalt von 200 g/L. An der Membrane 2 liegt im Hohlraum E Meerwasser mit einer Konzentration von 35 g/L an. Das Meerwasser diffundiert durch die Membrane 2 in die höherkonzentrierte Lösung in den Hohlraum C. Der Hohlraum C ist durch eine Rohrleitung mit dem Hohlraum D des Behälter B verbunden.In two containers A and B there are semi-permeable membranes that only allow E water and no salt. In the cavity C there is concentrated salt solution with a salt content of 200 g / L. Seawater with a concentration of 35 g / L is present in the cavity E on the membrane 2 . The sea water diffuses through the membrane 2 into the more concentrated solution into the cavity C. The cavity C is connected to the cavity D of the container B by a pipeline.
In den Hohlraum C des Behälters A baut das hereindiffundierte Wasser einen Druck auf. Dieser Druck wird auf die verschiebbare Membrane 7 übertragen und drückt normales Meerwasser, was sich vor der Membrane 7 befindet, durch die Membrane 2 des Behälters B. In den Hohlraum F des Behälter B bildet sich Süßwasser. Dieser Vorgang dauert nur so lange, bis sich die konzentrierte Salzlösung in den Behälter A im Hohlraum C verdünnt hat, und damit der osmotische Druck nachläßt.The water diffused into the cavity C of the container A builds up a pressure. This pressure is transferred to the displaceable membrane 7 and presses normal sea water, which is located in front of the membrane 7 , through the membrane 2 of the container B. Fresh water is formed in the cavity F of the container B. This process only lasts until the concentrated salt solution has diluted into the container A in the cavity C, and thus the osmotic pressure subsides.
Deshalb wird die verdünnte Lösung von Behälter A in den Hohlraum C durch die Pumpe 3 in das Flachbecken 4 geleitet, dort verdunstet durch die Einwirkung der Sonne ein Teil des Wassers der Lösung, und die Lösung wird aufkonzentriert. Ein anderer Teil der Lösung aus den Behälter A wird durch die Pumpe 3 in ein Gradierwerk gegeben.Therefore, the dilute solution of container A is passed into the cavity C by the pump 3 in the shallow pool 4 , where part of the water of the solution evaporates due to the action of the sun, and the solution is concentrated. Another part of the solution from the container A is given by the pump 3 in a graduation tower.
Dieses besteht aus einem rechteckigen Quader, in dem sich Dornreisig befindet. Die Breitseiten des Quaders werden dem Wind ausgesetzt, und die Lösung die von oben auf die Dornreiser gegeben wird, wird durch den Wind der das Wasser der Lösung verdunstet aufkonzentriert. Die aufkonzentrierte Lösung wird durch die Pumpe 3 wieder in den Hohlraum C des Behälters A gegeben. Wobei beachtet werden muß, daß sich in den Hohlraum D des Behälters B sich die Salzkonzentration des Meerwassers erhöht, wobei der Hohlraum B von Zeit zu Zeit mit frischem Meerwasser geflutet werden muß. Die Anlage ist wesentlich kostengünstiger als eine Destillationsanlage, kann jedoch mit einer Destillationsanlage gekoppelt werden, wenn Salzsohle anfällt.This consists of a rectangular cuboid with twigs in it. The broad sides of the cuboid are exposed to the wind, and the solution that is poured onto the thorn veins from above is concentrated by the wind that evaporates the water of the solution. The concentrated solution is returned to the cavity C of the container A by the pump 3 . It must be noted that the salt concentration of the sea water increases in the cavity D of the container B, the cavity B having to be flooded with fresh sea water from time to time. The plant is much cheaper than a distillation plant, but can be coupled to a distillation plant if the brine is required.
BezugszeichenlisteReference list
1 Behälter A und B
2 Halbdurchlässige Membranen
3 Pumpe
4 Flachbecken
5 Quaderförmiges Gestell
6 Auffangwanne für Salzsohle 1 container A and B
2 semipermeable membranes
3 pump
4 shallow pools
5 rectangular frame
6 collecting tray for salt sole
Claims (1)
Zur Aufrechterhaltung der Konzentration der Lösung dient ein Gradierwerk, das aus einen quaderförmigen Gestell besteht.
In dem Gestell befindet sich Dornreisig und wird mit den Breitseiten den Wind ausgesetzt. Die lösung wird von oben auf das Dornreisig gegeben, wo sie sich unter der Wirkung des Windes konzentriert. In einen Auffangbecken sammelt sie sich. Die vorkonzentrierte Lösung wird nun in ein Flachbecken gegeben, wo sie der Sonne ausgesetzt wird und ein Teil des Wassers der Lösung verdunstet und die Lösung wird konzentrierter. Ist der Konzentrationsgrad erreicht, so wird die konzentrierte Lösung in den Hohlraum des Behälters A gegeben wo sich der osmotische Druck wieder aufbaut.Solar seawater desalination plant, characterized in that there is a semipermeable membrane in each of two containers A and B. Concentrated salt solution is located in the cavity of one container and is connected to the cavity of container B by a pipeline. Sea water is located in front of the membrane of tank A. This diffuses through the membrane into the cavity of container A and builds up an osmotic pressure. This pressure is transferred to a movable membrane in the pipeline and presses sea water through the membrane of tank B. Fresh water is generated on this membrane.
To maintain the concentration of the solution, a graduation system is used, which consists of a rectangular frame.
Thorn twigs are in the frame and the broad sides are exposed to the wind. The solution is poured from above onto the twigs, where it is concentrated under the action of the wind. It collects in a catch basin. The pre-concentrated solution is now placed in a shallow basin where it is exposed to the sun and part of the water in the solution evaporates and the solution becomes more concentrated. When the degree of concentration is reached, the concentrated solution is added to the cavity of container A, where the osmotic pressure builds up again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19508821A DE19508821A1 (en) | 1995-03-11 | 1995-03-11 | Solar-powered sea water desalination |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19508821A DE19508821A1 (en) | 1995-03-11 | 1995-03-11 | Solar-powered sea water desalination |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE19508821A1 true DE19508821A1 (en) | 1995-10-05 |
Family
ID=7756412
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE19508821A Withdrawn DE19508821A1 (en) | 1995-03-11 | 1995-03-11 | Solar-powered sea water desalination |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE19508821A1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10000874A1 (en) * | 2000-01-12 | 2001-07-19 | Klaus Brinkmann | Emergency cross-flow water filter is contained within portable case and electrically powered by solar cells or wind generator |
| WO2005049500A1 (en) * | 2003-11-18 | 2005-06-02 | Söll Gmbh | Device and method for treating water with the aid of membranes |
| US8685252B2 (en) | 2010-02-04 | 2014-04-01 | Dxv Water Technologies, Llc | Water treatment systems and methods |
| US10513446B2 (en) | 2014-10-10 | 2019-12-24 | EcoDesal, LLC | Depth exposed membrane for water extraction |
-
1995
- 1995-03-11 DE DE19508821A patent/DE19508821A1/en not_active Withdrawn
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE10000874A1 (en) * | 2000-01-12 | 2001-07-19 | Klaus Brinkmann | Emergency cross-flow water filter is contained within portable case and electrically powered by solar cells or wind generator |
| WO2005049500A1 (en) * | 2003-11-18 | 2005-06-02 | Söll Gmbh | Device and method for treating water with the aid of membranes |
| US8685252B2 (en) | 2010-02-04 | 2014-04-01 | Dxv Water Technologies, Llc | Water treatment systems and methods |
| US8999162B2 (en) | 2010-02-04 | 2015-04-07 | Econopure Water Systems, Llc | Water treatment systems and methods |
| US10513446B2 (en) | 2014-10-10 | 2019-12-24 | EcoDesal, LLC | Depth exposed membrane for water extraction |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| OAV | Applicant agreed to the publication of the unexamined application as to paragraph 31 lit. 2 z1 | ||
| 8122 | Nonbinding interest in granting licences declared | ||
| 8139 | Disposal/non-payment of the annual fee |