DE3505026A1 - Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants - Google Patents

Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants

Info

Publication number
DE3505026A1
DE3505026A1 DE19853505026 DE3505026A DE3505026A1 DE 3505026 A1 DE3505026 A1 DE 3505026A1 DE 19853505026 DE19853505026 DE 19853505026 DE 3505026 A DE3505026 A DE 3505026A DE 3505026 A1 DE3505026 A1 DE 3505026A1
Authority
DE
Germany
Prior art keywords
scrubbing
liquid
scrubbing liquid
gas
washing
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Withdrawn
Application number
DE19853505026
Other languages
German (de)
Inventor
Heribert Dipl.-Ing. 4390 Gladbeck Dewert
Heinrich Ing.(grad.) 4600 Dortmund Gresch
Heinz Dipl.-Ing. Hölter
Heinrich Dipl.-Ing. 4390 Gladbeck Igelbüscher
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to DE19853505026 priority Critical patent/DE3505026A1/en
Priority to PCT/EP1986/000064 priority patent/WO1986004521A1/en
Priority to EP86901375A priority patent/EP0215039A1/en
Publication of DE3505026A1 publication Critical patent/DE3505026A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/60Simultaneously removing sulfur oxides and nitrogen oxides
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

Scrubber systems are known which contacted the gas with a very large amount of scrubbing water from a relatively large storage vessel, the scrubbing liquid being integrated in the scrubber system with respect to atmospheric oxygen excess. In order to prevent an influence on the scrubbing liquid for simultaneous scrubbing of NOx and SO2, according to the invention it is proposed that the scrubbing liquid is not contacted with the largest possible excess of atmospheric oxygen, as is the case in SO2 scrubbing, but the contact time with the excess of atmospheric oxygen is kept as short as possible during the NOx scrubbing, and the scrubbing liquid surfaces are available covered with respect to the untreated gas system (1) and/or the clean gas system (2) of the scrubber (6) integrated to the reservoir of the flue gas scrubbing. According to the apparatus, the chemical and/or electrolytic effects for the reductive adjustment of redox potential are carried out in a vessel system encapsulated with respect to the scrubbing process, the feed of the scrubbing liquid which has been in contact with the untreated gas being carried out via piping diameters which are adapted to the scrubbing liquid flow rate, which scrubbing liquid is preferably additionally introduced into the scrubbing liquid vessel equipment (4), which is separated from the untreated gas and/or clean gas, by submerged pipe feed systems. <IMAGE>

Description

Beschreibung und Erläuterung zur PatentanmeldungDescription and explanation of the patent application

"Verfahren und Vorrichtung zur Verhinderung der Beeinflussung der Waschflüssigkeit zur simultanen NOx und Restspuren-S02-Waschung durch Luftsauerstoff bei der Rauchgaswaschung hinter Verbrennungsanlagen"."Method and device for preventing the influence of the Scrubbing liquid for simultaneous NOx and residual trace S02 scrubbing using atmospheric oxygen in the case of flue gas scrubbing behind incineration plants ".

Zur Waschung von S02 und NO.x wird in neuerer Zeit nach den Patentanmeldungen Hölter eine zweistufige S02- und N0x-Waschung angewandt.For the washing of SO2 and NO.x is more recently according to the patent applications He used a two-stage S02 and N0x wash.

Die Waschflüssigkeitskreisläufe, die bevorzugt zur $02-Waschung angesetzt sind, benötigen eine oxidative Beeinflussung, um CaSO4 herzustellen beim Kalkverfahren.The washing fluid circuits, which are preferably set up for washing require an oxidative influence in order to produce CaSO4 in the lime process.

Die Waschflüssigkeit, die vorwiegend zur NO##Abscheidung dient, muß eine reduzierende Eigenschaft aufweisen, vorzugsweise ein negatives Redox-Potential von, je nach i'rO# und 502 Belastung und gewünschtem sowie erforderlichem Auswaschgrad von NO minus 50 bis minus 300 mV (gemessen gegen Kalomelelektrode).The washing liquid, which is mainly used for NO ## separation, must have a reducing property, preferably a negative redox potential from, depending on i'rO # and 502 load and desired and required Degree of leaching from NO minus 50 to minus 300 mV (measured against a calomel electrode).

Zur Aufrechterhaltung des negativen Redox-Potentials werden chemische Stoffe und/oder elektrolytische Einflüsse wirksam gemacht.To maintain the negative redox potential, chemical Substances and / or electrolytic influences made effective.

Es wurde gefunden, daß der Verbrauch an chemischen Zuschlagstoffen, wie Natriumdithionit und/oder zusätzlich elektrischer Energie für die Elektrolyse zur Einstellung des negativen Redox-Potentials nicht der Stickoxidbelastungswert im Rohgas darstellt, sondern der Luftsauerstoffüberschuß im Rohgas den Bedarf von chemischen Zuschlagstoffen und/oder elektrolytischer Energie sehr stark negativ wirtschaftlich beeinflußt.It has been found that the consumption of chemical additives, such as sodium dithionite and / or additional electrical energy for electrolysis to set the negative redox potential, not the nitrogen oxide exposure value represents in the raw gas, but the excess oxygen in the raw gas the demand of chemical additives and / or electrolytic energy very negative economically influenced.

Es wird daher erfindungsgemäß vorgeschlagen, den Luftsauerstoff so kurzzeitig wie möglich mit der Waschflüssigkeit zur NO -Auswaschun in Kontakt zu bringen.It is therefore proposed according to the invention, the atmospheric oxygen so briefly as possible with the Washing liquid for NO washing out to bring in contact.

Bisher wurden Wäschersysteme angewandt, die in einfachster Art und Weise mit einer sehr hohen Waschwassermenge aus einem relativ großen Vorratsbehälter das Gas in Kontakt brachten, und die Waschflüssigkeit ohne besondere Aufmerksamkeit gegenüber Luftsauerstoffüberschuß im Wäschersystem integriert wird.So far, scrubber systems have been used in the simplest manner and Way with a very large amount of washing water from a relatively large storage tank brought the gas into contact, and the scrubbing liquid without special attention against excess air oxygen is integrated in the scrubber system.

Brfindungsgemäß wird daher vorgeschlagen, die Waschflüssigkeit zur NO##Auswaschung so kurzzeitig wie möglich mit geringstem rengenwert von Waschflüssigkeitsmenge zur Rauchgasmenge mit dem Gas in Verbindung zu bringen, um den erforderlichen Auswaschgrad zu garantieren, wobei die Waschflüssigkeitsmenge so gering wie möglich bevorratet wird, daß immer nur die momentan notwendige Waschflüssigkeitsmenge fast kongruent zur Beaufschlagung mit dem Rohgas zur NO -Waschung mit negativem Redox-Potential versehen wird und die abfließende Waschflüssigkeitsmenge aus dem Hauptwäscher zur NO -Waschuna und/oder Vorwäscher bzw.According to the invention, it is therefore proposed to use the washing liquid NO ## Wash out as briefly as possible with the lowest possible amount of washing liquid to bring the amount of flue gas into contact with the gas in order to achieve the required degree of scrubbing to guarantee, with the amount of washing liquid stored as low as possible becomes that only the amount of washing liquid required at the moment is almost congruent for loading with the raw gas for NO scrubbing with negative Redox potential is provided and the amount of washing liquid flowing off from the Main washer for NO washing and / or pre-washer or

weiteren Waschstufen.in einen kleinen Waschvorratsmengenbehälter, vorzugsweise abtauchend in die Flüssigkeit eingeführt wird, und die Flüssigkeit selber gegen den Roh- und/oder bereits gewaschenen Reingasstrom abgedichtet zur Redox-Potential-Ein-Stellung durch chemische Zuschlagstoffe und/oder Elektrolyse im System integriert ist.further washing stages. in a small washing reservoir, is introduced into the liquid, preferably submerged, and the liquid itself sealed against the raw and / or already washed clean gas flow Redox potential on setting through chemical additives and / or electrolysis is integrated in the system.

Eine Vorrichtung zur Durchführung dieser erfindungsgemäßen Idee ist in der beiliegenden Zeichnung dargestellt: mit (1) das Rohgas; mit (2) das Reingas; mit (3) die Umlaufpumpe für die Waschflüssigkeit mit negativem Redox-Potential; mit (4) der erfindungsgemäß gegenüber dem Roh- und/ oder Reingasstrom abgedeckte Waschflüssigkeitsbehälter.mit abgetauchten Zuflußrohren aus den verschiedenen NO##Waschstufen (10); mit (5) ein Waschflüssigkeitsrohr aus Parallelwäschern; mit (6) der Wäscher; mit (7) die Düsen; mit (8) der Tropfenfänger im Reingassystem; mit (9) die Abdeckung der Waschflüssigkeit; mit (10) die abgetauchten Zuflußrohre aus den verschiedenen NO##Waschstufen.A device for implementing this inventive idea is shown in the accompanying drawing: with (1) the raw gas; with (2) the clean gas; with (3) the circulation pump for the washing liquid with negative redox potential; with (4) the one covered according to the invention with respect to the raw and / or clean gas stream Washing liquid container with submerged supply pipes from the various NO ## washing stages (10); with (5) a washing liquid pipe made up of parallel washers; with (6) the washer; with (7) the nozzles; with (8) the drip catcher in the clean gas system; with (9) the cover of the washing liquid; with (10) the submerged inflow pipes from the various NO ## washing stages.

Durch diese erfindungsgemäße Vorrichtung wird der erfindungsgemäße Gedanke erzielt, das Roh- und/oder Reingas, das zur NO -Waschung mit einer Waschflüssigkeit, die negatives Redox-Potential c?Ufweist und reduzierende Eigenschaften besitzt, so kurz wie möglich mit dem Gasstrom / Rohgasstrom in Verbindung zu bringen und die Waschflüssigkeitsbevorratung gegenüber dem Gasstrom abgedeckt zu nutzen.This inventive device is the inventive Thought achieved, the raw and / or clean gas that is used for NO scrubbing with a scrubbing liquid, has negative redox potential and has reducing properties, as briefly as possible with the gas flow / raw gas flow and to use the scrubbing liquid storage covered with respect to the gas flow.

Die Bevorratung der Waschflüssigkeit soll so klein bemessen sein, daß nach Herstellung des reduzierenden Redox-Fotentials die Waschflüssigkeit so schnell wie möglich mit dem Gasstrom in Kontakt gebracht wird, und diese Bevorratung nur wenige Minuten beträgt, um den Luftsauerstoff, der evtl. durch die Abtauchrohre in den Behälter gelangt, so gering wie möglich wirksam werden zu lassen.The storage of the washing liquid should be so small that that after making the reducing Redox Photentials the washing liquid is brought into contact with the gas flow as quickly as possible, and this storage only a few minutes to remove the oxygen from the air, which may have passed through the immersion tubes gets into the container to be effective as little as possible.

Die Abdeckung der Waschflüssigkeit wird vorzugsweise durch eine schwimmende wasser- und luftundurchlässige Schicht durchgeführt, die in der zugeschnittenen t'orm die Flbssigkeitsoberfläche schwimmend abdeckt, und nur die Öffnungen für die Waschflüssigkeitsrohre offen sind.The cover of the washing liquid is preferably by a floating water- and air-impermeable layer carried out in the tailored t'orm the liquid surface floating, and only the openings for the Washer fluid pipes are open.

Patentansprüche: - Leerseite -Patent claims: - blank page -

Claims (1)

Patentansprüche: Anspruch 1 Verfahren und Vorrichtung zur Verhinderung der Beeinflussunz der Waschflüssigkeit zur simultanen NOx- und S02-Waschung dadurch gekennzeichnet, daß die Waschflüssigkeit nicht, wie bei der S°2-Waschung, mit größtmöglichem Luftsauerstoffüberschuß kontaktiert wird, sondern die Kontaktzeit mit dem Luftsauerstoffüberschuß während der NO Waschung so gering wie möglich gehalten wird, und die Waschflüssigkeitsoberflächen abgedeckt gegenüber dem Roh- und/oder Reingassystem des Wäschers integriert zur Bevorratung der Rauchgaswaschung zur Verfügung stehen.Claims: Claim 1 method and device for prevention the influence of the scrubbing liquid for simultaneous NOx and S02 scrubbing as a result characterized that the washing liquid is not, as with the S ° 2 washing, with the greatest possible Air oxygen excess is contacted, but the contact time with the air oxygen excess is kept as low as possible during the NO washing, and the washing liquid surfaces covered against the raw and / or clean gas system of the washer integrated for Storage of the flue gas scrubbing are available. Anspruch 2 Verfahren und Vorrichtung zur Verhinderung der Beeinflussung der Waschflüssigkeit durch Luftsauerstoff nach Anspruch 1 dadurch gekennzeichnet, daß die Vorrichtung zur Durchführung des Verfahrens so ausgebildet ist, daß die chemischen und/oder elektrolytischen Einflüsse zur reduzierenden Redox-Potential-Einstellung in einem gegenüber dem Waschverfahren gekapselten Behältersystem durchgeführt wird, wobei die Zufuhr der mit dem Rohgas in Verbindung gestandenen Waschflüssigkeit über der Waschflüssigkeitsmenge angenaßte Rohrleitungsdurchmesser, die vorzugsweise zusätzlich in die gegenüber dem Roh- und/oder Reingas getrennten Waschflüssigkeitsbehältertechnik (4) durch abgetauchte Rohrzuflußsysteme eingeleitet werden, erfolgt.Claim 2 method and device for preventing the influence the washing liquid by atmospheric oxygen according to claim 1, characterized in that that the device for carrying out the method is designed so that the chemical and / or electrolytic influences for the reducing redox potential setting is carried out in a container system that is encapsulated compared to the washing process, wherein the supply of the scrubbing liquid in communication with the raw gas is carried out the amount of washing liquid wetted pipe diameter, which is preferably additionally in the washing liquid container technology, which is separate from the raw and / or clean gas (4) are introduced through submerged pipe inflow systems. Anspruch 3 Verfahren nach Anspruch 1 - 2 dadurch gekennzeichnet, daß die Waschflüssigkeitsmenge, die zur Waschung des Rohgasstromes genutzt wird, so kurzfristig wie möglich in kleinsten Vorratspartien mit reduzierender Eigenschaft versehen wird, und die Bevorratung so gemessen ist, daß die Verweilzeit im Bevorratungsbehälter zur Herstellung des reduzierenden negativen Redox-Potentials nur wenige Minuten beträgt - vorzugsweise kleiner 10 Minuten.Claim 3 Method according to Claim 1 - 2, characterized in that the amount of scrubbing liquid that is used to scrub the raw gas stream, see above short-term as possible in the smallest storage lots with reducing properties is provided, and the supply is measured so that the residence time in the storage container only a few minutes to produce the reducing negative redox potential is - preferably less than 10 minutes. Anspruch 4 Verfahren nach Anspruch 1 - 3 dadurch gekennzeichnet, daß die Abdeckung der Waschflüssigkeit durch eine schwimmende wasser- und luftundurchlässige Schicht erfolgt.Claim 4, method according to claims 1-3, characterized in that the cover of the washing liquid by a floating water and air impermeable Shift takes place.
DE19853505026 1985-02-07 1985-02-14 Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants Withdrawn DE3505026A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
DE19853505026 DE3505026A1 (en) 1985-02-14 1985-02-14 Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants
PCT/EP1986/000064 WO1986004521A1 (en) 1985-02-07 1986-02-06 Process for purifying combustion gases
EP86901375A EP0215039A1 (en) 1985-02-07 1986-02-06 Process for purifying combustion gases

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19853505026 DE3505026A1 (en) 1985-02-14 1985-02-14 Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants

Publications (1)

Publication Number Publication Date
DE3505026A1 true DE3505026A1 (en) 1986-08-14

Family

ID=6262483

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19853505026 Withdrawn DE3505026A1 (en) 1985-02-07 1985-02-14 Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants

Country Status (1)

Country Link
DE (1) DE3505026A1 (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2353528A1 (en) * 1972-10-25 1974-05-16 Hitachi Ltd Treating waste gases to remove nitrogen- and sulphur oxides - without the formation of nitric acid derivs
DE2416660A1 (en) * 1973-04-09 1974-10-24 Mitsui Petrochemical Ind PROCEDURE FOR THE REMOVAL OF NITROGEN OXYDE FROM A GAS
DE2460231A1 (en) * 1973-12-27 1975-07-03 Chisso Eng Co Ltd PROCESS FOR THE REMOVAL OF NITROGEN OXIDES FROM INDUSTRIAL EXHAUST GASES AND SUITABLE AQUATIC TREATMENT SOLUTIONS

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2353528A1 (en) * 1972-10-25 1974-05-16 Hitachi Ltd Treating waste gases to remove nitrogen- and sulphur oxides - without the formation of nitric acid derivs
DE2416660A1 (en) * 1973-04-09 1974-10-24 Mitsui Petrochemical Ind PROCEDURE FOR THE REMOVAL OF NITROGEN OXYDE FROM A GAS
DE2460231A1 (en) * 1973-12-27 1975-07-03 Chisso Eng Co Ltd PROCESS FOR THE REMOVAL OF NITROGEN OXIDES FROM INDUSTRIAL EXHAUST GASES AND SUITABLE AQUATIC TREATMENT SOLUTIONS

Similar Documents

Publication Publication Date Title
Kormann et al. Photolysis of chloroform and other organic molecules in aqueous titanium dioxide suspensions
US20230212042A1 (en) Use of electrochemical oxidation for treatment of per- and polyfluoroalkyl substances (pfas) in waste generated from sorbent and resin regeneration processes
JP3329456B2 (en) How to clean contaminated soil
EP0068458B1 (en) Process for treating continuous waste water streams containing variable contents of oxidizable compounds with hydrogen peroxide
Zirino et al. Measurement of copper and zinc in San Diego Bay by automated anodic stripping voltammetry
DE60218257T2 (en) METHOD OF WATER TREATMENT AND DEVICE THEREFOR
DE2523591A1 (en) PLANT FOR PURIFYING POLLUTED WATER
US3556970A (en) Treatment of effluents by the reverse osmosis process
EP1084002B1 (en) Method and system for cleaning semiconductor elements
EP0453706A2 (en) Detoxification of exhausted baths of photographic processes and washings by means of anodic oxidation
DE1954828B2 (en) Process for reducing mercury losses in chlor-alkali electrolysis using the amalgam process
DE3505026A1 (en) Process and apparatus for preventing the influence of atmospheric oxygen on the scrubbing liquid for simultaneous scrubbing of NOx and residual traces of SO2 in flue gas scrubbing downstream of combustion plants
DE2211890A1 (en) Waste water purification - using conc hydrogen peroxide forming nascent oxygen recombined for biological purification
DE69933997T2 (en) METHOD AND APPARATUS FOR DECONTAMINATING METALLIC SURFACES
JPS6218230B2 (en)
DE1642499C3 (en) Process for pool water treatment
DE10221362B4 (en) Process for the oxidation of sulphide dissolved in wastewater
DE19641018A1 (en) Treating waste water, e.g. from gas pipe washing
DE3224350A1 (en) Process for wet purification of contaminated exhaust air
DE9415140U1 (en) Plant for reducing pollutants in chlorinated water
DE3507626A1 (en) Process and apparatus for carrying out the process of separating out NOx downstream of already-installed flue gas scrubbers for separating out SO2 or flue gases which only have NOx pollution
DE1517634C (en) Process for detoxifying wastewater contaminated with hydrazine, dimethylhydrazine and nitrogen oxide
DE2341143A1 (en) Covering oxygen requirements of natural waters - by supplying hydrogen peroxide in concns. which do not harm micro-organisms
DE4433287A1 (en) Reducing pollution in water contg. e.g. chlorine
DE19955446A1 (en) Dosing unit acting as a reservoir discharges dissolved ingredient through membrane into surrounding flow of water under treatment

Legal Events

Date Code Title Description
OM8 Search report available as to paragraph 43 lit. 1 sentence 1 patent law
OP8 Request for examination as to paragraph 44 patent law
8139 Disposal/non-payment of the annual fee