DE2545862A1 - Thermal separation of solids from waste water - by evaporation in heated collecting tanks - Google Patents
Thermal separation of solids from waste water - by evaporation in heated collecting tanksInfo
- Publication number
- DE2545862A1 DE2545862A1 DE19752545862 DE2545862A DE2545862A1 DE 2545862 A1 DE2545862 A1 DE 2545862A1 DE 19752545862 DE19752545862 DE 19752545862 DE 2545862 A DE2545862 A DE 2545862A DE 2545862 A1 DE2545862 A1 DE 2545862A1
- Authority
- DE
- Germany
- Prior art keywords
- solids
- thermal separation
- waste water
- collecting tanks
- wastewater
- 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.)
- Pending
Links
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
- C02F1/048—Purification of waste water by evaporation
Landscapes
- 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)
Abstract
Description
Titel: Verfahren zur thermischen Trennung von FeststoffenTitle: Process for the thermal separation of solids
aus Abwasser. from sewage.
Anwendungsgebiet: Die Erfindung betrifft ein Verfahren zur thermischen Trennung von Feststoffen aus Abwasser wie sie z.B. bei Galvanikbetrieben, Beizereien und bestimmten Produktionen anfallen.Field of application: The invention relates to a method for thermal Separation of solids from wastewater, e.g. in electroplating plants, pickling plants and certain productions.
Zweck: Das Verfahren soll eine wirtschaftlishe, schadlose Vernichtung von Sonderabfällen in Abwässern aus Produktionen, Beizereien und Galvanikbetrieben ermöglichen Stand der Technik: Die Entgiftung von Abwässern mittels Ionenaustauschern und die Neutralisation auf chemischem Wege sind bekannte Verfahren um giftige Abwässer zu entgiften und Säuren und Laugen zu neutralisieren.Purpose: The procedure is intended to be an economic, harmless destruction of hazardous waste in wastewater from production, pickling and electroplating plants enable state-of-the-art technology: the detoxification of waste water using ion exchangers and chemical neutralization are known methods of toxic waste water to detoxify and to neutralize acids and alkalis.
Kritik des Standes der Technik: Die Entgiftung mittels Ionentauscher erfordert investitions und betriebskosteaufwendige Anlagen. Die Neutralisation und Spaltung auf chemischem Wege erfordert weitere Chemikalien und geschultes Fachpersonal.Criticism of the state of the art: detoxification using ion exchangers requires systems that are expensive to invest and operate. The neutralization and Chemical splitting requires additional chemicals and trained professionals.
Nach der Entgiftung muß das Wasser noch z.B. mittels Filterpressen von den festen Bestandteilen getrennt werden. Bei der chemischen Neutralisation müssen zusätzliche Chemikalien verwandt werden, die U.U. die Menge des Rückstandes noch erhöhen. After the detoxification, the water has to be filtered through a filter press, for example separated from the solid components. In chemical neutralization additional chemicals must be used, depending on the amount of residue still increase.
Eine Trennung der festen Bestandteile vom Wasser ist ein zusätzlicher Verfahrensgang. A separation of the solid components from the water is an additional one Procedure.
Aufgabe: Der Erfindung liegt die Aufgabe zugrunde die vorgenannten Nachteile der Entgiftung durch Ionentauscher sowie der chemischen Spaltung und Neutralisation aus Abwasser in didem Verfahrensgang wirtschaftlich zu ermöglichen.Task: The invention is based on the above-mentioned task Disadvantages of detoxification by ion exchangers as well as chemical splitting and neutralization economically from wastewater in the process.
Lösung: Die Aufgabe wird erfindungsmäßig dadurch gelöst, daß wässrige Abfallprodukte in beheizbaren Becken oder Tanks gesammelt werden. Durch Erhitzen der Flüssigkeiten über 100 Grad C wird das Wasser verdampft. Der Wasserdampf wird je nach Inhalt an Schadstoffen entweder direkt oder über Gaswäscher angesaugt und in die Atmosphäre abgeblasen.Solution: According to the invention, the object is achieved in that aqueous Waste products are collected in heated basins or tanks. By heating of liquids above 100 degrees C, the water is evaporated. The water vapor will Depending on the content of pollutants, either drawn in directly or via a gas scrubber and blown into the atmosphere.
Weitere tusgestaltung der Erfindung: Es wird zur Erwärmung bzw. Verdampfung der Flüssigkeit die anfallende Abwärme aus einer Müllverbrennungsanlage genutzt.Further design of the invention: It is used for heating or evaporation the waste heat from a waste incineration plant is used for the liquid.
Erzielbare Vorteile: Die mit der Erfindung erzielten Vorteile liegen vor allem darin, daß Sonderabfälle in flüssiger Form mit geringem Kostenaufwand in Wasserdampf und Feststoffen getrennt werden.Achievable Advantages: The advantages achieved with the invention are especially in the fact that hazardous waste is in liquid form at low cost separated into water vapor and solids.
Da in der Regel der Feststoffanteil solcher Abwässer unter 10 % liegt, wird die Menge, die schadlos vernichtet werden muß, erhilich reduziert. Since the solids content of such wastewater is usually below 10%, the amount that must be destroyed without damage is reduced accordingly.
Gegenüber den bekannten Verfahren erfolgt die Trennung in nur einem Verfahrensgang. Compared to the known processes, the separation takes place in only one Procedure.
is werden keine zusätzlichen Chemikalien zur Trennung benötigt. No additional chemicals are required for separation.
Die aus der Nüllverbrennungsanlage anfallende Wärmeenergie kann genutzt werden, Der Wasserdampf kann wieder kondensiert werden und als technisches Brauwasser Verwendung finden. The thermal energy from the waste incineration plant can be used The water vapor can be condensed again and used as technical brewing water Find use.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19752545862 DE2545862A1 (en) | 1975-10-14 | 1975-10-14 | Thermal separation of solids from waste water - by evaporation in heated collecting tanks |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19752545862 DE2545862A1 (en) | 1975-10-14 | 1975-10-14 | Thermal separation of solids from waste water - by evaporation in heated collecting tanks |
Publications (1)
Publication Number | Publication Date |
---|---|
DE2545862A1 true DE2545862A1 (en) | 1977-04-28 |
Family
ID=5959062
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19752545862 Pending DE2545862A1 (en) | 1975-10-14 | 1975-10-14 | Thermal separation of solids from waste water - by evaporation in heated collecting tanks |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE2545862A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0014648A1 (en) * | 1979-02-13 | 1980-08-20 | Edouard Paul Grenet | Process for the simultaneous and economic production of energy sources, fresh water and by-products from aqueous substances and an energy source |
-
1975
- 1975-10-14 DE DE19752545862 patent/DE2545862A1/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0014648A1 (en) * | 1979-02-13 | 1980-08-20 | Edouard Paul Grenet | Process for the simultaneous and economic production of energy sources, fresh water and by-products from aqueous substances and an energy source |
FR2474646A2 (en) * | 1979-02-13 | 1981-07-31 | Grenet Edouard | METHOD FOR SIMULTANEOUS AND PROFITABLE PRODUCTION OF ENERGY, FRESHWATER AND BY-PRODUCT SOURCES FROM AQUEOUS SUBSTANCES AND ENERGY SOURCE |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE3905924A1 (en) | METHOD FOR SEPARATING AND RECOVERING COMPONENTS FROM MIXTURES BY PERVAPORATION | |
DE1244747B (en) | Process for the extraction of ammonia from industrial waste water | |
DE3229903A1 (en) | Process and device for reprocessing a drying medium used for drying solvent-containing inks, paints, adhesives or the like on paper or comparable cellulose products | |
DE2545862A1 (en) | Thermal separation of solids from waste water - by evaporation in heated collecting tanks | |
EP0176963B1 (en) | Process and apparatus for the separation of a complexly composed load from liquid wastes such as industrial waste waters and sanitary landfill leachates | |
DE2346609A1 (en) | Concentration of encrusting liquids salt water or effluent - by mixing with liquid possessing higher affinity for tube surfaces | |
DE4030331C2 (en) | ||
DE3634666C2 (en) | ||
DE3610199A1 (en) | Process for cleaning soils contaminated with pollutants | |
DE2034372C3 (en) | Method and apparatus for treating separation vapor from the fractionation of tall oil | |
WO1991007353A1 (en) | Process for purifying organically polluted waste water | |
DE69930284T2 (en) | DEVICE FOR CLEANING A FLUID IN THE FORM OF STEAM FROM A CIRCULATION | |
DE2523973A1 (en) | PROCESS FOR THE PROCESSING OF WASTEWATER, IN PARTICULAR WASTE CONTAINING TOXIC SALES AND EQUIPMENT FOR CARRYING OUT THE PROCESS | |
DE3503199C2 (en) | Process for producing a soil improver or a fertilizer from sewage sludge | |
DE4333318A1 (en) | Process for working up oil-in-water emulsions | |
DE2218769C3 (en) | Process for cleaning up odorous waste water streams | |
DE2514862A1 (en) | METHOD FOR TREATMENT OF WATER CONTAINING PHENOLS | |
DE3710319A1 (en) | Process for the long-term and environmentally friendly disposal of industrial dusts having water-soluble fractions, in particular filter dust from refuse incineration plants | |
DE2304649A1 (en) | METHOD AND APPARATUS FOR THE SIMULTANEOUS INCINERATION OF COMBUSTIBLE WASTE AND SLUDGE | |
DE69205357T2 (en) | Method and device for disposing of liquid from the bottom of solid urban waste landfills. | |
DD260056A1 (en) | METHOD FOR THE TREATMENT AND REMOVAL OF DETECTED WATER EQUIPMENT OF WASTE DEPONY | |
DE2653792A1 (en) | Polluting process waste gas elimination furnace - uses gas from oil and water mixt. in combustion chamber to burn toxic waste gases | |
EP0204078A3 (en) | Process for purifying chlorinated aliphatic polymers | |
DE2632811A1 (en) | Industrial wastes deodorisation - by introducing air at specified pressure in counterflow to scrubber column | |
DE1810630C (en) | Process and method for separating the constituents of "oil in water" old emulsions |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
OHJ | Non-payment of the annual fee |