DE102008059064A1 - Decalcification system for sea water and residual/waste products from a desalination system, comprises self-regenerating ion exchange materials - Google Patents
Decalcification system for sea water and residual/waste products from a desalination system, comprises self-regenerating ion exchange materials Download PDFInfo
- Publication number
- DE102008059064A1 DE102008059064A1 DE102008059064A DE102008059064A DE102008059064A1 DE 102008059064 A1 DE102008059064 A1 DE 102008059064A1 DE 102008059064 A DE102008059064 A DE 102008059064A DE 102008059064 A DE102008059064 A DE 102008059064A DE 102008059064 A1 DE102008059064 A1 DE 102008059064A1
- Authority
- DE
- Germany
- Prior art keywords
- sea water
- residual
- ion exchange
- waste products
- desalination
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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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
- C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
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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
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
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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
- Y02A20/131—Reverse-osmosis
Abstract
Description
Diese Erfindung beschreibt eine Methode des Meerwasserabbauverfahrens mit Nullabsonderung. Sie kann als alleiniges Verfahren oder an jeder bereits bestehenden Entsalzungsanlage angebracht werden.These Invention describes a method of seawater degradation process with zero separation. It can be as a sole procedure or at everyone already existing desalination plant.
Diese Erfindung wird als ”Meerwasserabbauverfahrens mit Nullabsonderung” genannt. Sie gehört zur Entsalzungsprozessen der technischen der Desalinationen.These Invention is called "seawater degradation process with zero separation "called. she belongs for desalination processes of technical desalinations.
Der bekannte Stand der Technik ist das bisher bewährte Entsalzung des Meerwassers mit Reversosmosis (RO). Diese RO-Technik findet einen breiten Einsatz.Of the known prior art is the previously proven desalination of seawater with reverse osmosis (RO). This RO technique is widely used.
Dabei wird es vom 100% Meerwasser-Input ca. 42% Trinkwasser produziert. Mehr als 58% salzkonzentriertes Meerwasser kehrt mit mehr als 1,7-fachen Salzgehalt zurück ins Meer. Also ein wachsendes Umweltproblem der Meeresflora.there it is produced by the 100% seawater input about 42% drinking water. More than 58% salt-concentrated seawater returns more than 1.7 times Salinity back into the sea. So a growing environmental problem of the marine flora.
An den RO-Anlagen stellt das Kalziumkarbonat und andere Härtekomponenten ein beachtliches Problem mit starker Funktionseinschränkung mit Reduktion der Desalinationsmembranpermeabilität dar. Deshalb werden Chemikalien zur Lösung des Wasserhärteproblems benutzt.At The RO plants provides the calcium carbonate and other hardness components a significant problem with severe functional limitation with That's why chemicals are used to the solution the water hardness problem used.
Es finden weiter verschiedene Typen der Entsalzungsanlagen der Thermodesalinationstechniken, wie MSF ”Multi stage flash”, MED ”Multi effect dissillation” und VC ”Vapor compression” Anwendung. Mansche Desalinationsanlagen besteht aus Kombination dieser Typen. Der dabei gewonnene Frischwasseranteil ist kleiner als 47%. Also mehr als 53% Salzwasserkonzentrate kehren ins Meer zurück. Es kommt zu einer Erhöhung der Salzkonzentration um 1,8fache. Ähnliche Problematik wie bei der RO-Anlagen.It find further different types of desalination plants of thermal desalination techniques, like MSF "Multi stage flash ", MED "Multi effect dissipation "and VC "Vapor compression "application. Some desalination systems consist of a combination of these types. The amount of fresh water gained is less than 47%. So more than 53% salt water concentrates return to the sea. It comes to an increase the salt concentration by 1.8 times. Similar problematic as with the RO facilities.
Alle diese industriell eingesetzten Desalinationsprozesse sind eindeutig nicht umweltfreundlich. Sie verursachen eine enorme Verschmutzung des Meereslebens. Durch die weltweit eingesetzten Wasserentsalzungsanlagen werden ca. 9 qkm im Jahr (9 000 000 m3/J) konzentriertes Salzwasser an die Küstenregionen ohne irgendwelche Behandlung abgegeben. Es entsteht eine zunehmende ökologische Dysbilanz mit unabsehbaren Folgen.All These industrially used desalinization processes are clear not environmentally friendly. They cause enormous pollution of marine life. Through the worldwide used water desalination plants 9 sq km per year (9,000,000 m3 / yr) of concentrated salt water to the coastal regions delivered without any treatment. It creates an increasing ecological Dysbilanz with unforeseeable consequences.
Um eine umweltfreundliche ökologische effektive Problemlösung dieser Entsalzungstechniken hat sich die IES-Germany über viele Jahre intensiver Arbeit bemüht.Around an environmentally friendly ecological effective problem-solving This desalination techniques has the IES Germany many Years of intensive work.
Mit der Erfindung des Meerwasserabbauverfahrens mit Null-Absonderung (Zero-Discharge) meiner Firma ”IES” konnten wir das Entsalzungsproblem auf eine ökologische und kommerziell ökonomische Ebene effektiv lösen.With the invention of the zero-segregation seawater degradation process (Zero-discharge) my company "IES" could we put the desalination problem on an ecological and commercial economic level effectively solve.
Dabei wird das Trinkwasser out-put gewonnene Anteil stark erhöht und das hochkonzentrierte Salzwasser mit selbst-regenerierenden Dekalzifizierungsprozessen (gilt für Meerwasser und den Resten/Abfallprodukten aus den Entsalzungsanlagen) in autonomer Technik durchgeführt.there The drinking water out-put gained share is greatly increased and that highly concentrated salt water with self-regenerating decalcification processes (applies to Seawater and the residues / waste products from the desalination plants) carried out in autonomous technique.
Es werden neben den potentiell vollständiger Trinkwassergewinnung die im salzwassergelösten Substanzen (Kalzium-, Magnesium-, Kalium-, Natriumsalzen) in Kristaliner Form mit niedrigem Energieverbrauch separat (pur) getrennt.It Beyond the potentially complete drinking water production the substances dissolved in salt water (Calcium, magnesium, potassium, sodium salts) in crystal form separated separately (pure) with low energy consumption.
Diese Substanzen sowie seltene Mineralien, die im Konzentrat ins Meer zurück befördert werden, werden mit unserer Erfindung mit dem Ziel einer Null-Absonderung bearbeitet. Die Umweltbelastung wird dadurch signifikant verringert.These Substances and rare minerals that are in the concentrate in the sea back promoted Become, with our invention with the goal of a zero-separation processed. The environmental impact is thereby significantly reduced.
Die erzielten Vorteile sind nunmehr zu benennen:
- 1. Keine umweltbelastenden Rückständen mehr aus den noch im Einsatz sich befindenden Entsalzungsanlagen
- 2. Kostengünstige Energieverfahren mit ökologischem und ökonomischem Vorteil
- 3. Keine Chemikalieneinsätze durch die selbst-regenerierenden Prozesse
- 4. Gewinnung von Mineralien und Salzen in purer Form
- 5. Das Trinwasser ou-put gewonnene Anteil wird auf das Maximum erhöht
- 6. Die Lebensdauer der Entsatzungsanlage wird deutlich verlängert (Desalinationsmembrane geschont)
- 7. Das globale Wasserproblem auf unserem Planet kann noch effektiver ausgelöst werden
- 8. Die Bewässerung verschienen Gebiete kann kommerziell günstig erfolgen. Eine Bevölkerung und Bewohnung solcher Gebiete mit Vegetation kann möglich werden.
- 1. No more polluting residues from the still in use desalination plants
- 2. Cost-effective energy processes with ecological and economic advantage
- 3. No use of chemicals due to self-regenerating processes
- 4. Production of minerals and salts in pure form
- 5. Proportion won from the Trinwasser ou-put is increased to the maximum
- 6. The lifetime of the Entsatzungsanlage is significantly extended (Desalinationmembrane spared)
- 7. The global water problem on our planet can be triggered even more effectively
- 8. Irrigation varied areas can be commercially favorable. A population and habitation of such areas with vegetation can become possible.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008059064A DE102008059064A1 (en) | 2008-11-26 | 2008-11-26 | Decalcification system for sea water and residual/waste products from a desalination system, comprises self-regenerating ion exchange materials |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008059064A DE102008059064A1 (en) | 2008-11-26 | 2008-11-26 | Decalcification system for sea water and residual/waste products from a desalination system, comprises self-regenerating ion exchange materials |
Publications (1)
Publication Number | Publication Date |
---|---|
DE102008059064A1 true DE102008059064A1 (en) | 2010-05-27 |
Family
ID=42114659
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE102008059064A Withdrawn DE102008059064A1 (en) | 2008-11-26 | 2008-11-26 | Decalcification system for sea water and residual/waste products from a desalination system, comprises self-regenerating ion exchange materials |
Country Status (1)
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DE (1) | DE102008059064A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102011012805A1 (en) * | 2011-03-02 | 2012-09-06 | I-E-S E.K., Inhaber Dr. Oliver Jacobs | Treatment of raw brine from desalination plants |
-
2008
- 2008-11-26 DE DE102008059064A patent/DE102008059064A1/en not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102011012805A1 (en) * | 2011-03-02 | 2012-09-06 | I-E-S E.K., Inhaber Dr. Oliver Jacobs | Treatment of raw brine from desalination plants |
DE102011012805B4 (en) * | 2011-03-02 | 2013-06-06 | I-E-S E.K., Inhaber Dr. Oliver Jacobs | Treatment of raw brine from seawater desalination plants |
US9487424B2 (en) | 2011-03-02 | 2016-11-08 | I-E-S E.K., Inhaber Dr. Oliver Jacobs | Treatment of raw brines from desalination plants |
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ON | Later submitted papers | ||
OP8 | Request for examination as to paragraph 44 patent law | ||
8130 | Withdrawal | ||
8165 | Unexamined publication of following application revoked |