DE2749886A1 - Salt load disposal in flue gas desulphurisation plant - by spraying saturated wash water upstream of electrofilter - Google Patents
Salt load disposal in flue gas desulphurisation plant - by spraying saturated wash water upstream of electrofilterInfo
- Publication number
- DE2749886A1 DE2749886A1 DE19772749886 DE2749886A DE2749886A1 DE 2749886 A1 DE2749886 A1 DE 2749886A1 DE 19772749886 DE19772749886 DE 19772749886 DE 2749886 A DE2749886 A DE 2749886A DE 2749886 A1 DE2749886 A1 DE 2749886A1
- Authority
- DE
- Germany
- Prior art keywords
- flue gas
- wash water
- salt load
- electrofilter
- water upstream
- 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.)
- Ceased
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/74—Cleaning the electrodes
- B03C3/78—Cleaning the electrodes by washing
Abstract
Description
Beschreibung und Erläuterung zur PatentanmeldungDescription and explanation of the patent application
' Verfahren zur Ausschleusung der Salzfracht für Rauchgas-Wascnanlagen, vorzugsweise bei Entscnwefelungsanlagen von Kraftwerken und Müllverbrennungsentsorgungsanlaqen, aus dem Waschflüssigkeitskrelslauf'.'' Procedure for discharging the salt load for flue gas washing systems, preferably in desulphurisation plants of power plants and waste incineration disposal plants, from the washing liquid flow '.
Es ist bekannt, daß insbesonders bei einem Einsatz von Kohle mit hohem Kalziumcnloridgenalt eine Aufsalzung der Wascnflüssigkeit bis auf 30 % möglich ist und somit zwangsläufig ein Ablassen der Waschflüssigkeit aus dem Kreislauf notwendig wird, um ein Übersalzen des Waschflüssigkeitskreislaufes zu vermeiden.It is known that especially when using coal with high Calcium chloride usually increases the salt content of the washing liquid up to 30% and thus inevitably draining the washing liquid from the circuit is necessary in order to avoid over-salting of the washing liquid circuit.
Die abzulassende Wascnflüssigkeit muß entweder durch einen Sprühtrockner benandelt werden, um die Salzfracht auszufällen, um das Wasser dem Kreislauf wieder zuzuführen, oder in die Vorflut abgegeben werden.The washing liquid to be drained off must either go through a spray dryer can be modified to precipitate the salt load to bring the water back into the cycle to be supplied or discharged into the receiving water.
Eine weitere Möglichkeit besteht, das Abwasser entsprecnend zu verdünnen, um es dann in die Vorflut zu geben.Another possibility is to dilute the wastewater accordingly, to then give it to the receiving water.
Beide notwendigen Verfahrensschritte sind sehr stark kostenbelastend für das Verfahren.Both of the necessary process steps are very costly for the procedure.
Aus diesem Grunde wird erfindungsgemäß vorgeschlagen, ein Verfahren zur Ausschleusung der Salzfracht aus dem Wascnkrelslauf bei Rauchgaswäschen, vorzugsweise hinter Kraftwerken, wie folgt zu gestalten Das Rauchgas tritt mit etwa 180 - 2200C in den Elektrofilter ein, um entstaubt zu werden.For this reason, a method is proposed according to the invention for discharging the salt load from the wascnkrelslauf with flue gas scrubbing, preferably behind power plants, to be designed as follows The flue gas occurs at around 180 - 2200C into the electrostatic precipitator to be dedusted.
Hinter dem Elektrofilter wird das auf etwa 150 mg/Nm3 Staubgehalt gereinigte Raucngas der nassen Rauchgasentschwefelungsanlage zugeführt.Behind the electrostatic precipitator, this is reduced to around 150 mg / Nm3 dust content cleaned flue gas fed to the wet flue gas desulphurisation system.
Erfindungsgemäß wird die erforderliche Flüssigkeit mit der entsprechenden Salzfracht vor dem Elektrofilter eingesprüht, das Wasser verdunstet und der Salzgenalt mit dem Staub agglomeriert wodurch zwangsläufig noch eine Verbesserung der Leitfähigkeit der abzuscheidenden Stäube erzielt wird, so daß der Wirkungsgrad des E lektrofilters sich verbessert und gleichzeitig das Problem der Salzfrachtausschleusung durch diese erfindungsgemäße Maßnahme gelöst ist.According to the invention, the required liquid with the appropriate Salt load sprayed in front of the electrostatic precipitator, the water evaporates and the salt content agglomerated with the dust, which inevitably leads to an improvement in conductivity the dust to be separated is achieved, so that the efficiency of the electric filter improves and at the same time the problem of salt cargo discharge through them measure according to the invention is solved.
Selbstverständlich ist die Erfindung nicht auf die vorstehend im einzelnen beschriebenen Ausbildungsformen beschränkt, sondern es sind zahlreiche Abänderungen möglich, ohne jedoch son dem ßrundqerlanken abzuweichen, bei einer Rauchgaswässtwe aus dem Waschflüssigkeitskreislauf die überscnüssige Salzfracht in den Heißgasbereich vor dem Elektrofilter einzudüsen, das Wasser zu verdampfen und die Salzfracht zwangsläufig zur Agglomeration des Staubes und Abscheidung in einem Abscheider zu erzielen.Of course, the invention is not limited to the above in detail The forms of training described are limited, but there are numerous changes possible, but without deviating from the round cross-section, in the case of a flue gas water the excess salt load from the scrubbing liquid circuit into the hot gas area to be injected in front of the electrostatic precipitator, the water to evaporate and the salt load inevitably to achieve agglomeration of the dust and separation in a separator.
Patentanspruch Claim
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19772749886 DE2749886A1 (en) | 1977-11-08 | 1977-11-08 | Salt load disposal in flue gas desulphurisation plant - by spraying saturated wash water upstream of electrofilter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19772749886 DE2749886A1 (en) | 1977-11-08 | 1977-11-08 | Salt load disposal in flue gas desulphurisation plant - by spraying saturated wash water upstream of electrofilter |
Publications (1)
Publication Number | Publication Date |
---|---|
DE2749886A1 true DE2749886A1 (en) | 1979-05-10 |
Family
ID=6023264
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19772749886 Ceased DE2749886A1 (en) | 1977-11-08 | 1977-11-08 | Salt load disposal in flue gas desulphurisation plant - by spraying saturated wash water upstream of electrofilter |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE2749886A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2929974A1 (en) * | 1979-07-20 | 1981-02-12 | Leisegang Umwelttechnik Kg | Incinerator and cupola furnace gases purification - in pre-absorber, cyclones, venturi scrubber and oxidation basin for dust and toxic gas removal |
US6379639B2 (en) * | 1998-08-17 | 2002-04-30 | Jürgen Labuschewski | Process for purification of flue gas |
EP2889089A1 (en) * | 2013-12-27 | 2015-07-01 | Windhager Zentralheizung Technik GmbH | Method and apparatus for cleaning an electrofilter |
-
1977
- 1977-11-08 DE DE19772749886 patent/DE2749886A1/en not_active Ceased
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2929974A1 (en) * | 1979-07-20 | 1981-02-12 | Leisegang Umwelttechnik Kg | Incinerator and cupola furnace gases purification - in pre-absorber, cyclones, venturi scrubber and oxidation basin for dust and toxic gas removal |
US6379639B2 (en) * | 1998-08-17 | 2002-04-30 | Jürgen Labuschewski | Process for purification of flue gas |
EP2889089A1 (en) * | 2013-12-27 | 2015-07-01 | Windhager Zentralheizung Technik GmbH | Method and apparatus for cleaning an electrofilter |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
8110 | Request for examination paragraph 44 | ||
8131 | Rejection |