EP0293424A1 - PROCEDE DE REDUCTION DE L'EMISSION DE NO x? PAR LES CHAUFFERIES - Google Patents

PROCEDE DE REDUCTION DE L'EMISSION DE NO x? PAR LES CHAUFFERIES

Info

Publication number
EP0293424A1
EP0293424A1 EP19870907928 EP87907928A EP0293424A1 EP 0293424 A1 EP0293424 A1 EP 0293424A1 EP 19870907928 EP19870907928 EP 19870907928 EP 87907928 A EP87907928 A EP 87907928A EP 0293424 A1 EP0293424 A1 EP 0293424A1
Authority
EP
European Patent Office
Prior art keywords
flue gas
proviso
fine particles
suspension
power plant
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Withdrawn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
EP19870907928
Other languages
German (de)
English (en)
Inventor
Georg Gebhard
Heinz HÖLTER
Ernst-Peter Dr. Uerpmann
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.)
Holter Heinz Dipl-Ing
Original Assignee
Holter Heinz Dipl-Ing
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 Holter Heinz Dipl-Ing filed Critical Holter Heinz Dipl-Ing
Publication of EP0293424A1 publication Critical patent/EP0293424A1/fr
Withdrawn legal-status Critical Current

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
    • B01D53/54—Nitrogen compounds
    • B01D53/56—Nitrogen oxides

Definitions

  • the invention relates to a method for reducing NO emissions of flue gases from combustion plants.
  • NO is a collective term for the different oxides of nitrogen, especially nitrogen monoxide
  • Nitrogen dioxide is generally less than 5 percent by volume and is largely formed on the way from the combustion system to the chimney outlet.
  • NO limit values were determined, which are also calculated as NO «in mg / m 3 R X.
  • the lowering of the oxygen concentration and / or the combustion temperature in the flame area are known, for example, as primary firing measures.
  • the secondary measures include methods of reducing the NOx Verbindunq 3 e 'n into nitrogen (N "), the gas remains in the flue gas, or oxidation of the nitrogen monoxide to Stickstoff ⁇ dioxide, which is dissolved in aqueous phase and in the form of nitrate by-product arises.
  • ammonia (NHject) is burned in excess at temperatures between 850 ° and 1000 ° C, the reduction of nitrogen monoxide being faster than the combustion of ammonia. Part of the excess ammonia reacts with oxygen to form nitrogen Substance and water, the rest of it enters the atmosphere in downstream systems and possibly via the chimney.
  • a disadvantage of all processes is that sometimes complex and expensive special systems have to be set up.
  • a disadvantage is above all that simultaneous separation of nitrogen and sulfur oxides is not possible. Rather, the systems are usually connected in series.
  • the invention is based on the object of specifying a possibility for reducing NO emissions from flue gases from combustion plants, which results in the lowest possible NO emissions, the aim being preferably at the same time to use a simultaneous SO p - Combine cleaning of the flue gases.
  • the invention is based on the knowledge that a drastic reduction in the NO content in the flue gas stream can be achieved by a sufficient number of free Surfaces of very fine particles are made available within the washing suspension of the flue gas desulfurization system, namely those very fine particles which are suitable for absorbing and / or adsorbing nitrogen oxides on their surface or for reacting with them.
  • the proportion of very fine particles (suspended matter) in the washing suspension must be kept deliberately low (preferably zero).
  • the prior art assumes that this is the only way that the formation of the calcium sulfate hydrate products is not adversely affected or that no dewatering problems occur.
  • the state of the art has hitherto always assumed that only the desulfurization of the flue gases is carried out in the flue gas desulfurization system, namely by absorption of the sulfur dioxide from the flue gases with the aid of appropriate absorption agents (for example limestone), this process being as little as possible to be disturbed.
  • the method according to the invention is characterized by the features of claim 1.
  • Advantageous further developments result from the features of the claims and the other application documents.
  • Various materials have proven to be particularly advantageous.
  • clays and clay minerals may be mentioned, in particular those from the smectite, vermiculite and / or mica group relate hu ⁇ giller other silicates, and hydrates thereof, for example, volcanic rocks or the like.
  • the corresponding very fine particles can be added as such to a conventional washing suspension, for example a limestone washing suspension, or can be prepared to a suspension with water.
  • waste materials from limestone processing which may also contain fumed or silicate components, have also proven to be suitable.
  • unburned constituents for example from wet ash, coarse ash and / or fly ash, enable a power plant firing to have the desired effect.
  • Wet ash is understood to mean an exhausted kettle ash which has unburned heavy particles.
  • coarse ash in unleached ashes.
  • the coarse ash essentially consists of quartz, silicates such as clays or mica, calcium oxide and unburned coal.
  • the flue gas scrubber in order to optimize the NO bond, it is proposed to recycle the flue gas scrubber, that is to say to increase the proportion of very fine particles within the scrubbing suspension or, in other words, to thicken the scrubbing suspension.
  • the fine particle content can be increased and adjusted so that the " best possible NO binding is achieved.
  • only an excess material flow is then withdrawn from the circulating water of the desulfurization system.
  • the circulating water should preferably be run with a proportion of the fine particles above 50 ml / l, this proportion being able to be increased up to 1000 ml / l, with higher solids contents preferred in the sense of a NO ⁇ reduction in the flue gas stream become.
  • the proportion of very fine particles, based on the total washing medium can preferably be at least 5% by weight or, according to an advantageous embodiment of the invention, up to 100% by weight.
  • the degree of separation of the nitrogen oxides can be increased.
  • trace elements such as iron, manganese, chromium, copper, nickel, cobalt, zinc, lead, strontium and / or boron salts in the aqueous phase are improved, obviously they also influence the oxidation of nitrogen oxides in a catalytic manner.
  • the trace elements can be added separately to the washing suspension, but in some cases they can also be introduced via the impurities in the limestone used as an absorption medium for desulfurization.
  • the degree of separation of NO or N0 ? is otherwise improved if the temperature of the aqueous phase is set to above 45 ° C, preferably between 45 ° and 65 ° C.
  • the pH of the wash suspension should also preferably be between 4 and 7.
  • the invention has also recognized that the degree of oxidation in the flue gas is important in relation to the reduction of NO emissions from flue gases from combustion plants has.
  • the degree of oxidation is the volume ratio of nitrogen dioxide to the sum of nitrogen monoxide and nitrogen dioxide (multiplied by 100). Accordingly, in an advantageous embodiment, which can also be seen as an alternative, the invention proposes to set the degree of oxidation of the flue gas to a value between 5% and 50%. Measures for this are given below as examples.
  • the degree of oxidation can be adjusted by both primary and secondary measures.
  • firing measures of a known type are suitable, such as the use of low-NO ⁇ burners in the combustion system or the reduction in the combustion temperature of the flue gases.
  • N0 ? it is particularly advantageous to use nitrogen-containing compounds, in particular ammonia, to form N0 ? to burn.
  • nitrogen-containing compounds in particular ammonia
  • urea, NH.0H, liquid manure or municipal sewage sludge can also be burned to form 0 p , which has the advantage that problem or residual material is simultaneously removed in this way.
  • N0p then obviously reacts additionally to NO to form nitrous oxide (N p 0 "), which is in the water (in the washing suspension) with the formation of nitrate (NO.) or nitrite (N0 ? ) is relatively easily soluble, the nitrite then reacting with HS0 "to form various NS compounds, from which nitrogen (N") and sulfate are then formed is, the latter reacting with the Ca ions of the wash suspension to calcium sulfite / calcium sulfate products.
  • NO. nitrate
  • N0 ? nitrite
  • the invention also proposes further manipulations of the wash suspension.
  • the washing suspension should contain hydrogen peroxide (H p O p )
  • Eberiso can be added to ozone to oxidize the nitrogen oxides.
  • nitrates as alkali and / or alkaline earth nitrates, preferably calcium and / or sodium nitrates in solid and / or liquid form to admit.
  • nitrates as alkali and / or alkaline earth nitrates, preferably calcium and / or sodium nitrates in solid and / or liquid form to admit.
  • the separation of the nitrogen oxides is further improved by adding nitrogen-containing compounds, such as ammonium salts or urea, which are NH 3 , NH ⁇ H, (NH 4 ) 2 S0 4 , NH..CL, (NH 4 ) N0 3 , NH 4 CL, (NH 4 ) p _CO 3 and / or (NH 2 ) 2 CO in solid and / or dissolved form are added, the NO p with these substances being known in a manner known per se, in particular within the preferred temperature range of the washing suspension converts to nitrogen.
  • a smaller proportion of NH can also be introduced directly via the exhaust gas.
  • the method according to the invention leads to a reduction of the NO emissions by up to 90 percent, depending on the type and amount of the catalysts used and / or adsorbent / adsorbent.

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)

Abstract

Procédé de réduction de l'émission de NOx accompagnant les gaz brûlés, par mise en contact du jet de gaz avec des microparticules tensio-actives.
EP19870907928 1986-12-18 1987-12-04 PROCEDE DE REDUCTION DE L'EMISSION DE NO x? PAR LES CHAUFFERIES Withdrawn EP0293424A1 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE3643343 1986-12-18
DE3643343 1986-12-18
DE19873729482 DE3729482A1 (de) 1986-12-18 1987-09-03 Verfahren zur reduzierung von no(pfeil abwaerts)x(pfeil abwaerts)-emissionen von rauchgasen aus feuerungsanlagen
DE3729482 1987-09-03

Publications (1)

Publication Number Publication Date
EP0293424A1 true EP0293424A1 (fr) 1988-12-07

Family

ID=25850533

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19870907928 Withdrawn EP0293424A1 (fr) 1986-12-18 1987-12-04 PROCEDE DE REDUCTION DE L'EMISSION DE NO x? PAR LES CHAUFFERIES

Country Status (3)

Country Link
EP (1) EP0293424A1 (fr)
DE (1) DE3729482A1 (fr)
WO (1) WO1988004571A1 (fr)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1989011329A1 (fr) * 1988-05-16 1989-11-30 Roland Fichtel Agent et procede pour purifier des gaz et des gaz d'echappement, et procede pour produire ledit agent
EP0454885A1 (fr) * 1990-05-02 1991-11-06 Ftu Gmbh Procédé pour la purification de gaz et de gaz d'échappement de polluant
BE1015841A3 (fr) † 2003-12-24 2005-10-04 Lhoist Rech & Dev Sa Composition pulverulente a base d'un compose calco-magnesien.

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5710769B2 (fr) * 1974-06-03 1982-02-27
DE3335543A1 (de) * 1983-09-29 1985-04-18 Wolfgang 1000 Berlin Meuser Duesenanordnung zur anwendung fuer die reinigung von schmutzgas

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO8804571A1 *

Also Published As

Publication number Publication date
WO1988004571A1 (fr) 1988-06-30
DE3729482A1 (de) 1988-06-30

Similar Documents

Publication Publication Date Title
DE69324365T2 (de) VERFAHREN ZUR ENTFERNUNG VON NOx AUS GASEN DER VERBRENNUNSZONE DURCH ABSORPTION
DE3854728T2 (de) Methode zum Entfernen von NOx- und SOx-Emissionen aus Verbrennungssystemen unter Verwendung stickstoffhaltiger Verbindungen.
EP0234188B1 (fr) Procédé d'épuration de gaz d'échappement contenant des oxydes d'azote et du soufre dans des installations de combustion
DE2705901C3 (de) Verfahren zum Entfernen von Schwefeloxiden und ggf. Stickstoffoxiden aus sauerstoffhaltigen Abgasen
EP0314733B1 (fr) Utilisation d'hydroxyde de calcium reactif pour la purification de gaz et de gaz d'echappement
EP0377010A1 (fr) Agent et procede pour purifier des gaz et des gaz d'echappement, et procede pour produire ledit agent
EP0276883B1 (fr) Procédé de dénitration et de désulfuration simultanées d'un gaz d'échappement contenant de l'oxygène
US3987146A (en) Simultaneous removal of nitrogen oxides and sulfur oxides from combustion gases
EP0123856B1 (fr) Procédé d'élimination ou d'isolation de polluants de gaz d'échappement
WO1984004053A1 (fr) Procede et installation de purification des gaz de combustion provenant par exemple de chauffages domestiques, de moteurs a combustion ou de chauffages similaires
DE3031286C2 (de) Verfahren zum Behandeln von staub- und schwefeloxidhaltigem Rauchgas
DD268404A1 (de) Verfahren zum entfernen von so tief x und no tief x aus rauchgas
DE102012012367B4 (de) Aktivierter trass,dessen herstellung und verwendung
EP1406719B1 (fr) Procede de traitement de gaz de fumee contenant de l'ammoniac
DE2504027A1 (de) Verfahren zur entfernung von stickoxiden aus abgasen
EP0293424A1 (fr) PROCEDE DE REDUCTION DE L'EMISSION DE NO x? PAR LES CHAUFFERIES
EP0350963A2 (fr) Procédé pour la réduction des émissions de SO2 et/ou de NOX dans les procédés de combustion
EP0682974A2 (fr) Procédé pour la dénitration d'un gaz d'échappement
US3630943A (en) Preparation of absorbents for sulfur oxide removal
DE19756392A1 (de) Verfahren und Katalysator zur Entfernung von Stickoxiden aus Abgasen von Zementofenanlagen und von Verbrennungsprozessen
EP0399404A2 (fr) Procédé pour réduire les émissions de SO2 et/ou NOx dans les procédés de combustion
DE4039014C2 (de) Verfahren zur Herstellung und Anwendung eines Mittels zur Senkung des Calciumsulfatgehaltes in Lösungen
DE1963618C3 (de) Verfahren zur Entfernung von Schwefeldioxyd aus Rauchgas oder Abgas
DE19652902A1 (de) Verfahren zum Entfernen von Ammoniak oder Aminen, sowie deren Abbauprodukten aus Abgasen, insbesondere Abgasen einer Verbrennung
DE2000059C3 (de) Verfahren zur Entschwefelung von Verbrennungsgasen

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE FR GB IT LI LU NL SE

17P Request for examination filed

Effective date: 19880721

RIN1 Information on inventor provided before grant (corrected)

Inventor name: GEBHARD, GEORG

Inventor name: UERPMANN, ERNST-PETER, DR.

Inventor name: HOELTER, HEINZ

17Q First examination report despatched

Effective date: 19891219

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 19900830