EP0862019A1 - Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille - Google Patents

Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille Download PDF

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Publication number
EP0862019A1
EP0862019A1 EP97810110A EP97810110A EP0862019A1 EP 0862019 A1 EP0862019 A1 EP 0862019A1 EP 97810110 A EP97810110 A EP 97810110A EP 97810110 A EP97810110 A EP 97810110A EP 0862019 A1 EP0862019 A1 EP 0862019A1
Authority
EP
European Patent Office
Prior art keywords
dusts
ash
incinerator
high temperature
grate
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.)
Granted
Application number
EP97810110A
Other languages
German (de)
English (en)
Other versions
EP0862019B1 (fr
Inventor
Bruno Carcer
John Millard
Verena Dr. Schmidt
Adrian Dr. Selinger
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.)
Martin GmbH fuer Umwelt und Energietechnik
Original Assignee
ABB Research Ltd Switzerland
ABB Research Ltd Sweden
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 ABB Research Ltd Switzerland, ABB Research Ltd Sweden filed Critical ABB Research Ltd Switzerland
Priority to EP97810110A priority Critical patent/EP0862019B1/fr
Priority to DE59709100T priority patent/DE59709100D1/de
Priority to ES97810110T priority patent/ES2191163T3/es
Priority to DK97810110T priority patent/DK0862019T3/da
Priority to JP10045022A priority patent/JPH10246416A/ja
Priority to NO19980843A priority patent/NO314673B1/no
Publication of EP0862019A1 publication Critical patent/EP0862019A1/fr
Application granted granted Critical
Publication of EP0862019B1 publication Critical patent/EP0862019B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/002—Incineration of waste; Incinerator constructions; Details, accessories or control therefor characterised by their grates
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/32—Incineration of waste; Incinerator constructions; Details, accessories or control therefor the waste being subjected to a whirling movement, e.g. cyclonic incinerators
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00—Combustion
    • F23G2202/10—Combustion in two or more stages
    • F23G2202/104—Combustion in two or more stages with ash melting stage
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00—Combustion
    • F23G2202/10—Combustion in two or more stages
    • F23G2202/106—Combustion in two or more stages with recirculation of unburned solid or gaseous matter into combustion chamber
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00—Specific waste
    • F23G2209/30—Solid combustion residues, e.g. bottom or flyash
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2217/00—Intercepting solids
    • F23J2217/10—Intercepting solids by filters
    • F23J2217/102—Intercepting solids by filters electrostatic

Definitions

  • the invention relates to the field of waste incineration. It affects one Method and device for the thermal treatment of airborne dust and possibly fine ash from rust incineration plants.
  • a method is known from DE 38 11 820 A1, in which waste in a pyrolysis reactor in carbonization gas and in essentially non-volatile pyrolysis residues is converted.
  • the carbonization gas is then a separate one Afterburner supplied, as well as the fine fraction (smoked coke and Fine dust) of the residues and those in the dust filter system or in the heat recovery steam generator accruing fly ash (dust).
  • the dust and the fine particles are burned in this high temperature chamber and the solid parts melted.
  • the molten slag is then removed from the combustion chamber passed a water container, where it solidifies into a glass-like granulate.
  • AshArc furnace is designed for very large throughputs, it is possible to the fine fraction of the grate ash (approx. 8% of the waste used) together with the filter ash from the particle separation of the flue gas cleaning (approx. 2.5% of waste used).
  • the invention tries to avoid all of these disadvantages. You have the task based, a method and an apparatus for the thermal treatment of Fly dusts and possibly fine ash from waste incineration plants develop with those in a simple manner and at low cost Product is generated, which either slammed into the grate ash or else can be recycled separately and thus the remaining amount of fly ash is reduced becomes.
  • this is achieved in that in a method according to the preamble of claim 1 at least part of the dusts in the High temperature range of the incinerator is fed back, the Temperature in said high temperature range above the melting temperature or sintering temperature of the airborne dusts, and that the airborne dusts are in the high temperature range of the incinerator remain sufficiently long so that they at least partially glazed or sintered. These products can then added to the grate ash or recycled separately.
  • this is the case with a device according to the preamble of Claim 13 achieved in that the ash conveyor up to close the high temperature area of the incinerator extends that of the ash conveyor there a metering device for introducing at least one Part of the returned dusts in the high temperature area of the incinerator is connected downstream and that in the high temperature area of the incinerator Means to ensure a sufficient dwell time of the ashes are arranged.
  • the advantages of the invention include the elimination of separate ones High-temperature combustion chamber or the external furnace unit, which were previously used Melting of the fly ash was necessary. This can save costs will.
  • the product can be added to the grate ash so that the remaining amount of fly ash with a high proportion of pollutants compared to State of the art is reduced.
  • Another advantage of the invention is that existing systems can be easily retrofitted.
  • the dusts after discharge from the boiler or the dust filter system first into a low-pollutant and a pollutant-rich fraction are separated and only that Low pollutant fraction of the airborne dust in the high temperature area of the incinerator is recycled because it produces a low-pollutant product and the risks of corrosion problems from increased concentrations Heavy metals in the boiler area can be reduced.
  • the dusts are removed after discharge from the boiler or the dust separator with the fine fraction ( ⁇ 2 mm), for example
  • the dryEx / DryRec process dry discharge and dry sorting
  • the fine fraction ⁇ 2 mm
  • the dryingEx / DryRec process dry discharge and dry sorting
  • the melting properties e.g. B. viscosity, Melting temperature, the liquid slag improves, and it becomes a dry, but hardly any dusty rust ash.
  • Fig. 1 shows schematically a waste incineration plant according to a first embodiment the invention.
  • the waste incineration plant essentially consists of an incinerator 1, a boiler 2 and a dust collector 3, z. B. an electrostatic filter, are connected downstream.
  • a combustion grate 4 is arranged in the incinerator 1, on which the waste 5, for example household waste, with the supply of primary air 6 in the primary combustion chamber 7 is burned. The combustion takes place in the secondary combustion chamber 8 further completed due to the supply of secondary air 9.
  • flue dusts 10 which are associated with the flue gas 11 via the primary combustion chamber 7, the secondary combustion chamber 8, the radiation train 12 and the contact trains 13 of the boiler 2 in the boiler 2 and in the filter 3 be shipped.
  • the fly dusts 10 are on the boiler tube walls, not shown here, and the E-filter plates.
  • discharge devices also not shown here, such as cellular wheel locks or double flaps that Airborne dusts 10 from an ash conveyor system 14, preferably a trough chain conveyor, a pneumatic conveyor or a screw conveyor.
  • the ash conveyor 14 extends close to the high temperature area of the incinerator 1.
  • the ash conveyor 14 is one Dosing device 15, for. B. a plug screw or a piston pump, downstream.
  • the total dust 10 discharged is in this first Embodiment of the invention via the ash conveyor 14, if necessary with the addition of additives 16, for example water or melting point lowering Substances supplied to the metering device 15.
  • the additives 16, if any, are mixed Airborne dusts 10 metered into the high temperature range of the incinerator 1. If the ash (flue dust 10) was added to water 1 before being returned to the oven, so the already cooling effect of the recycled ash is on the surrounding refractory bricks of the incinerator 1 are reinforced. In order to a contribution is made to reducing corrosion. As can be clearly seen in FIG. 1 is in this primary embodiment, the dust 10 in the primary combustion chamber 7 returned.
  • the Airborne dusts 10 can be traced back to the high temperature region of the secondary combustion chamber 8 (see Fig. 2). It is crucial that the temperature in this area is higher than the melting temperature or the sintering temperature of the dusts 10 or the mixture of dusts 10 and additives 16, and that the residence time the dusts 10 or the mixture of dusts 10 and additives 16 is so large in this high-temperature region of the incinerator 2, that glazing or sintering of at least some of the dusts 10 takes place. It is particularly favorable if the entire proportion of the returned Product is melted or sintered. Shouldn't the temperatures may be sufficient, via support burner 17 (not shown here), which by means of Oil, gas or waste operations are operated, an additional amount of heat supplied will.
  • Means 18 arranged to ensure a sufficient residence time of the ashes.
  • These means 18 can, for example, channels, crucibles, baffles and or Slabs, but also specially shaped refractory bricks.
  • the products created during glazing / sintering slammed the grate ash 19, either dry or over a water bath is discharged wet from the incinerator 1.
  • the discharge is dry it is important that the ash discharge provides an airtight seal for the combustion chamber forms what is guaranteed in conventional systems by a water lock is.
  • the grate ash 19 is then via methods known per se, for. Legs Dry sorting, further processed.
  • Fig. 2 shows a second embodiment of the invention. It differs from the first embodiment only in that the dusts 10 after their Discharge from the boiler 2 and the filter 3 via the ash conveyor 14 in one Bunker 20 temporarily stored, then transported to a pelletizing plant 21 and then the pelletized dusts 10, if necessary again mixed with additives 16, in the high temperature range of the secondary combustion chamber 8 can be introduced in doses.
  • the schematically indicated in Fig. 2 external temperature source 17 (burner, burner lance) can the secondary combustion chamber 8 additionally supply thermal energy. This will in everyone If a temperature is guaranteed that is above the melting or sintering temperature the dusts 10 or the mixture of dusts 10 and additives 16 lies, so that the melting / sintering of the ash is supported.
  • Airborne dusts 10 are returned to the high-temperature region of the primary combustion chamber 7. Before being introduced into the combustion chamber 7, the flying dust 10 gets in a separation chamber 22, in which the dust 10 in a low-pollutant fraction 10.1 and be separated into a pollutant-rich fraction 10.2. Only the low pollutant Fraction 10.1 is on the ash conveyor 14 and the metering device 15 returned to the high temperature area of the incinerator 1 and slammed after the glazing of the grate ash 19.
  • Fig. 4 an embodiment of the invention is shown schematically, the differs from the first exemplary embodiment described in FIG. 1 only as a result distinguishes that the dusts 10 after discharge from the boiler 2 and the Filter 3 together with a fraction of the grate ash 19.1, which is smaller than 2 mm and was separated from the rest of the grate ash 19.2 in the sorting system 23 (e.g. at approx. 2 mm grain size), in the high temperature area of the incinerator 1 can be returned.
  • a fraction of the grate ash 19.1 which is smaller than 2 mm and was separated from the rest of the grate ash 19.2 in the sorting system 23 (e.g. at approx. 2 mm grain size)
  • FIG. 5 shows a possible embodiment of the in the high temperature range in the primary combustion chamber 7 or arranged in the secondary combustion chamber 8 Means 18 for ensuring a sufficient dwell time of the dusts 10.
  • the stuffing screw 15 is followed by a channel 18 in which the dusts 10 can stay under high temperature conditions for so long that at least partly melt and glaze or sinter and these products can then be slammed into the grate ash 19 or else be recycled separately.
  • FIG. 6 shows a further exemplary embodiment.
  • the firebox is 7.8 Afterburner 26 downstream, which is designed so that the melted Ash 25 can be discharged separately from the grate ash 19.
  • a mixture or a single fraction of the ash (boiler ash, Filter ash, fine fraction of the rust ash) with or without the addition of additives 16 in the combustion chamber 7,8 or the afterburning chamber 26 can be returned.
  • Another advantage of this design is the ability to get the dust over the nozzles for the secondary air 9 and / or tertiary air 24 in the hot area attributed.
  • a vortex flow can be generated in the afterburning chamber 26.
  • the vortex leads to better separation of the ash particles on the walls of the afterburner 26.
  • the recycled ash which by means of the secondary air 9 or Tertiary air 24 is introduced into the afterburner 26 is against the walls thrown, where an ash melt flow caused by the very high temperatures arises.
  • the molten ash 25 flows through the walls of the high temperature afterburner 26 down and is about a specially designed Device 27 removed from the afterburner 26.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
EP97810110A 1997-02-28 1997-02-28 Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille Expired - Lifetime EP0862019B1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP97810110A EP0862019B1 (fr) 1997-02-28 1997-02-28 Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille
DE59709100T DE59709100D1 (de) 1997-02-28 1997-02-28 Verfahren und Vorrichtung zur thermischen Behandlung von Flugstäuben aus Rostverbrennungsanlagen
ES97810110T ES2191163T3 (es) 1997-02-28 1997-02-28 Procedimiento y dispositivo para el tratamiento termico de polvos volatiles procedentes de instalaciones de incineracion con parrilla.
DK97810110T DK0862019T3 (da) 1997-02-28 1997-02-28 Fremgangsmåde og indretning til termisk behandling af flyveaske fra ristforbrændingsanlæg
JP10045022A JPH10246416A (ja) 1997-02-28 1998-02-26 火格子燃焼設備に由来するフライダストを熱的に処理するための方法と装置
NO19980843A NO314673B1 (no) 1997-02-28 1998-02-27 Fremgangsmåte og anordning for termisk behandling av flyvestöv fra ristforbrenningsanlegg

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP97810110A EP0862019B1 (fr) 1997-02-28 1997-02-28 Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille

Publications (2)

Publication Number Publication Date
EP0862019A1 true EP0862019A1 (fr) 1998-09-02
EP0862019B1 EP0862019B1 (fr) 2003-01-08

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP97810110A Expired - Lifetime EP0862019B1 (fr) 1997-02-28 1997-02-28 Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille

Country Status (6)

Country Link
EP (1) EP0862019B1 (fr)
JP (1) JPH10246416A (fr)
DE (1) DE59709100D1 (fr)
DK (1) DK0862019T3 (fr)
ES (1) ES2191163T3 (fr)
NO (1) NO314673B1 (fr)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002086389A1 (fr) * 2001-04-19 2002-10-31 Ebara Corporation Appareil et procede de traitement des dechets
EP1348905A1 (fr) * 2002-03-27 2003-10-01 MARTIN GmbH für Umwelt- und Energietechnik Procédé de traiter les résidues d'incinération d'un installation d'incinération
EP1348906A1 (fr) * 2002-03-27 2003-10-01 MARTIN GmbH für Umwelt- und Energietechnik Procédé d'influencer la qualité de résidues d'incinération d'une installation d'incinération
EP1348907A1 (fr) 2002-03-27 2003-10-01 MARTIN GmbH für Umwelt- und Energietechnik Procédé de diminuer le concentration des substances toxiques organiques dans les cendres volantes
EP1359374A1 (fr) * 2002-03-27 2003-11-05 MARTIN GmbH für Umwelt- und Energietechnik Procédé de traitement de résidues d'une installation d'incinération
SG126759A1 (en) * 2002-03-27 2006-11-29 Mitsubishi Heavy Ind Ltd Method for treatment of the residues of combustionresidues produced by combustion plant
EP1751468A2 (fr) * 2004-05-14 2007-02-14 Eco Technologies, LLC Chambre de combustion inclinée à manque d'air pour foyer
EP2128523A2 (fr) * 2008-05-29 2009-12-02 MARTIN GmbH für Umwelt- und Energietechnik Installation de combustion et procédé de réglage d'une installation de combustion
US7640872B2 (en) 2004-10-14 2010-01-05 Martin GmbH für Umwelt- und Energietechnik Process for influencing the properties of combustion residue
EP2085693A3 (fr) * 2008-01-31 2016-03-16 Anton Maggale Procédé et dispositif de combustion de combustibles solides
EP2426414A3 (fr) * 2010-09-06 2016-03-16 Egon Ruß Procédé et dispositif de combustion de combustibles solides
EP2746661A3 (fr) * 2012-12-21 2017-11-29 Andritz AG Installation de combustion
CN111068446A (zh) * 2019-12-27 2020-04-28 北京中航泰达环保科技股份有限公司 烧结烟气循环系统及烧结烟气循环系统清灰方法

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101005082B1 (ko) 2010-02-26 2010-12-30 한국기계연구원 석면 폐기물 처리 장치
CN110369451B (zh) * 2019-07-22 2021-01-29 中南大学 一种烧结机头灰与垃圾焚烧飞灰协同综合利用的方法

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1181360B (de) * 1959-10-16 1964-11-12 Siemens Ag Verfahren und Anlage zur Muellverbrennung in einem Dampferzeuger
DE3324627A1 (de) * 1983-07-08 1985-01-24 Müllverbrennungsanlage Wuppertal GmbH, 5600 Wuppertal Verfahren zum verbrennen von muell
DE3915992A1 (de) * 1988-05-19 1989-11-23 Theodor Koch Verfahren zur reduktion von stickstoffoxiden
EP0359209A2 (fr) * 1988-09-14 1990-03-21 John M. Kent Procédé et appareil d'utilisation de déchets dangereux pour former de l'agrégat non dangereux
WO1993017280A1 (fr) * 1992-02-26 1993-09-02 Kuenstler Hans Procede de fusion de residus de combustion dans des scories
EP0610114A1 (fr) * 1993-02-04 1994-08-10 T.I.R.U.- Traitement Industriel Des Residus Urbains Procédé d'incinération de combustibles solides, notamment résidus urbains, à rejets solides et gazeux sensiblement neutres vis-à-vis de l'environnement
DE4333510C1 (de) * 1993-10-01 1995-01-12 Gutehoffnungshuette Man Verfahren und Vorrichtung zur Behandlung von Rauchgasen aus Abfallverbrennungsanlagen

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1181360B (de) * 1959-10-16 1964-11-12 Siemens Ag Verfahren und Anlage zur Muellverbrennung in einem Dampferzeuger
DE3324627A1 (de) * 1983-07-08 1985-01-24 Müllverbrennungsanlage Wuppertal GmbH, 5600 Wuppertal Verfahren zum verbrennen von muell
DE3915992A1 (de) * 1988-05-19 1989-11-23 Theodor Koch Verfahren zur reduktion von stickstoffoxiden
EP0359209A2 (fr) * 1988-09-14 1990-03-21 John M. Kent Procédé et appareil d'utilisation de déchets dangereux pour former de l'agrégat non dangereux
WO1993017280A1 (fr) * 1992-02-26 1993-09-02 Kuenstler Hans Procede de fusion de residus de combustion dans des scories
EP0610114A1 (fr) * 1993-02-04 1994-08-10 T.I.R.U.- Traitement Industriel Des Residus Urbains Procédé d'incinération de combustibles solides, notamment résidus urbains, à rejets solides et gazeux sensiblement neutres vis-à-vis de l'environnement
DE4333510C1 (de) * 1993-10-01 1995-01-12 Gutehoffnungshuette Man Verfahren und Vorrichtung zur Behandlung von Rauchgasen aus Abfallverbrennungsanlagen

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002086389A1 (fr) * 2001-04-19 2002-10-31 Ebara Corporation Appareil et procede de traitement des dechets
EP1489356A1 (fr) * 2001-04-19 2004-12-22 Ebara Corporation Méthode et dispositif de traitement des déchets
EP1348905A1 (fr) * 2002-03-27 2003-10-01 MARTIN GmbH für Umwelt- und Energietechnik Procédé de traiter les résidues d'incinération d'un installation d'incinération
EP1348906A1 (fr) * 2002-03-27 2003-10-01 MARTIN GmbH für Umwelt- und Energietechnik Procédé d'influencer la qualité de résidues d'incinération d'une installation d'incinération
EP1348907A1 (fr) 2002-03-27 2003-10-01 MARTIN GmbH für Umwelt- und Energietechnik Procédé de diminuer le concentration des substances toxiques organiques dans les cendres volantes
EP1359374A1 (fr) * 2002-03-27 2003-11-05 MARTIN GmbH für Umwelt- und Energietechnik Procédé de traitement de résidues d'une installation d'incinération
DE10213787C1 (de) * 2002-03-27 2003-11-27 Martin Umwelt & Energietech Verfahren zum Minimieren der Konzentration an toxischen organischen Schadstoffen in Flugstäuben
SG126759A1 (en) * 2002-03-27 2006-11-29 Mitsubishi Heavy Ind Ltd Method for treatment of the residues of combustionresidues produced by combustion plant
EP1751468A2 (fr) * 2004-05-14 2007-02-14 Eco Technologies, LLC Chambre de combustion inclinée à manque d'air pour foyer
EP1751468A4 (fr) * 2004-05-14 2009-02-25 Eco Technologies Llc Chambre de combustion inclinée à manque d'air pour foyer
US7640872B2 (en) 2004-10-14 2010-01-05 Martin GmbH für Umwelt- und Energietechnik Process for influencing the properties of combustion residue
EP2085693A3 (fr) * 2008-01-31 2016-03-16 Anton Maggale Procédé et dispositif de combustion de combustibles solides
EP2128523A2 (fr) * 2008-05-29 2009-12-02 MARTIN GmbH für Umwelt- und Energietechnik Installation de combustion et procédé de réglage d'une installation de combustion
EP2128523A3 (fr) * 2008-05-29 2014-09-24 MARTIN GmbH für Umwelt- und Energietechnik Installation de combustion et procédé de réglage d'une installation de combustion
US8939094B2 (en) 2008-05-29 2015-01-27 Martin GmbH fuer Umwelt—und Energietechnik Incineration plant and method for controlling an incineration plant
EP2426414A3 (fr) * 2010-09-06 2016-03-16 Egon Ruß Procédé et dispositif de combustion de combustibles solides
EP2746661A3 (fr) * 2012-12-21 2017-11-29 Andritz AG Installation de combustion
CN111068446A (zh) * 2019-12-27 2020-04-28 北京中航泰达环保科技股份有限公司 烧结烟气循环系统及烧结烟气循环系统清灰方法
CN111068446B (zh) * 2019-12-27 2023-07-25 北京中航泰达环保科技股份有限公司 烧结烟气循环系统及烧结烟气循环系统清灰方法

Also Published As

Publication number Publication date
NO980843D0 (no) 1998-02-27
NO314673B1 (no) 2003-04-28
DE59709100D1 (de) 2003-02-13
JPH10246416A (ja) 1998-09-14
NO980843L (no) 1998-08-31
ES2191163T3 (es) 2003-09-01
DK0862019T3 (da) 2003-04-22
EP0862019B1 (fr) 2003-01-08

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