EP1348906A1 - Procédé d'influencer la qualité de résidues d'incinération d'une installation d'incinération - Google Patents

Procédé d'influencer la qualité de résidues d'incinération d'une installation d'incinération Download PDF

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Publication number
EP1348906A1
EP1348906A1 EP03001180A EP03001180A EP1348906A1 EP 1348906 A1 EP1348906 A1 EP 1348906A1 EP 03001180 A EP03001180 A EP 03001180A EP 03001180 A EP03001180 A EP 03001180A EP 1348906 A1 EP1348906 A1 EP 1348906A1
Authority
EP
European Patent Office
Prior art keywords
combustion
residues
slag
sintered
fuel
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
EP03001180A
Other languages
German (de)
English (en)
Other versions
EP1348906B1 (fr
Inventor
Johannes Martin
Oliver Dr. Gohlke
Joachim Horn
Michael Busch
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
Mitsubishi Heavy Industries Ltd
Original Assignee
Martin GmbH fuer Umwelt und Energietechnik
Mitsubishi Heavy Industries Ltd
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Publication date
Application filed by Martin GmbH fuer Umwelt und Energietechnik, Mitsubishi Heavy Industries Ltd filed Critical Martin GmbH fuer Umwelt und Energietechnik
Publication of EP1348906A1 publication Critical patent/EP1348906A1/fr
Application granted granted Critical
Publication of EP1348906B1 publication Critical patent/EP1348906B1/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
    • F23G5/50—Control or safety arrangements
    • 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
    • F23G5/006—General arrangement of incineration plant, e.g. flow sheets
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/60—Separating
    • F23G2201/602—Separating different sizes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00—Combustion
    • F23G2202/20—Combustion to temperatures melting waste
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/30—Oxidant supply
    • 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
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/50206—Pelletising waste before combustion

Definitions

  • the invention relates to a method for influencing the properties of combustion residues from a Incineration plant, in particular a waste incineration plant, where the fuel is on a grate burned and the resulting combustion residues by appropriate combustion control on a elevated temperature are brought.
  • molten Combustion residues Due to the high temperatures in the treatment of Combustion residues in a smelting stage are molten Combustion residues due to low levels of organic Marked connections. While typical Slags from waste incineration plants still unburned, usually measured as loss on ignition, from 1 to 5% by weight show the loss on ignition of molten combustion residues at below 0.3 wt .-%. In addition, are molten Combustion residues due to small proportions characterized by leachable salts and heavy metals, because these either evaporated or in the case of cooling the Melt forming glass matrix are involved.
  • the object of the invention is the combustion process so too influence and regulate that completely sintered Slag with the desired quality without the use of downstream melting or glazing units obtained becomes.
  • a "completely sintered slag" becomes a material understood that consists of sintered and / or melted chunks, typically a grain size of at least 2 to 8 mm. These chunks consist of combustion residues of garbage by complete or superficial Melting are agglomerated.
  • the sintered or smelted pieces may be due to gas release during sintering or melting quite a porous Have structure.
  • the possible porosity of the fully sintered Slag is due to the fact that the temperature the molten slag in the fuel bed is not high is enough to have a sufficiently low viscosity and thus to cause expulsion of gas bubbles, which in the Glass technology is also referred to as Läutern. This is different the completely sintered slag of typical vitrified slags that are in downstream high-temperature process in crucible furnaces lined with refractory material or other melt aggregates.
  • the fully sintered slag can also constituents of waste, such as glass or metals, containing of the combustion process largely unaffected the Walk through grate, so in the narrower sense in the fuel bed neither melted nor sintered, but in terms of Burnout and leachable pollutants the desired properties have.
  • Residual slag will be the slag constituents below not sintered and / or melted are. Residual slag is characterized by a comparison to completely sintered slag smaller grain size as well higher loss on ignition and proportion of leachable pollutants.
  • the above task is based on a Method of the type described above according to the invention solved by the fact that the combustion control so led that is already in the fuel bed of the main combustion zone a sintering and / or melting the Combustion residue to slag takes place, and that still not or not completely sintered or molten Combustion residue at the end of the combustion process deposited and fed to the combustion process again become.
  • the basic idea of the invention is thus, on the one hand to influence the combustion process on the grate so that already a sintering and / or melting process the firing grate takes place in the main combustion zone, and that each still not sintered or molten Incineration residues are returned, at the second or third pass the desired Sintering and / or melting experience.
  • the focus of the inventive concept is therefore the sintering and / or melting process of the combustion residues already in the fuel bed of the main combustion zone, which was not thought possible until now. It is namely for mechanical firing grates extremely harmful, if liquid slag between the individual grate bars or Other movable parts of the Feuerungsrostes arrives. Out For this reason one has a melting of the slag on the Avoided rust and made sure that in the fuel bed the Melting temperature of the slag is not reached.
  • the sintering and / or Melting process in the upper part of the fuel bed instead, because from the top the largest heat effect by the Radiation of the flame body takes place and from below by supplying relatively cold primary combustion air the Temperature of the directly on the Feuerungsrost lying Material can be kept lower than on the top of the fuel bed. Because with such a combustion control not the entire incipient combustion residues in a completely sintered slag with the desired Quality can be converted, those are Combustion residue, which does not yet have the character of completely sintered slag, the combustion process fed again.
  • an oxygen enrichment of the primary combustion air to about 25 vol .-% to 40 vol .-% is made.
  • Another advantageous measure is that a preheating the primary air temperature to values of approx. 100 ° C to 400 ° C is performed. These measures may vary depending on Conditions are used separately or combined. Preferably, depending on the nature of the Burning the fuel bed temperature in the main combustion zone set to 1,000 ° C to 1,400 ° C.
  • the separation of not completely sintered from the completely sintered slag is by classifying the Slag after discharge from the combustion system possible by making a separation cut at a grain size from e.g. 2 to 10 mm lays.
  • the oversize corresponds to the completely sintered slag, while the undersized represents the fraction to be recycled.
  • the separation can be done either by sieving or in further advantageous embodiment of the invention by a combination of sieves and a washing process done.
  • the fine fraction with a particle size of less than 2 to 10 mm is returned to the combustion process. there can return by adding to the given Fuel or by immediate task on the Burning bed done. To avoid dust formation and Improvement of the handling ability can precede the fine fraction the return be pelletisisert or briquetted.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Incineration Of Waste (AREA)
  • Regulation And Control Of Combustion (AREA)
EP03001180A 2002-03-27 2003-01-21 Procédé d'influencer la qualité de résidues d'incinération d'une installation d'incinération Expired - Lifetime EP1348906B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10213788 2002-03-27
DE10213788A DE10213788B4 (de) 2002-03-27 2002-03-27 Verfahren zur Beeinflussung der Eigenschaften von Verbrennungsrückständen aus einer Verbrennungsanlage

Publications (2)

Publication Number Publication Date
EP1348906A1 true EP1348906A1 (fr) 2003-10-01
EP1348906B1 EP1348906B1 (fr) 2005-08-10

Family

ID=27798211

Family Applications (1)

Application Number Title Priority Date Filing Date
EP03001180A Expired - Lifetime EP1348906B1 (fr) 2002-03-27 2003-01-21 Procédé d'influencer la qualité de résidues d'incinération d'une installation d'incinération

Country Status (11)

Country Link
US (1) US6748882B2 (fr)
EP (1) EP1348906B1 (fr)
CN (1) CN100352554C (fr)
AT (1) ATE301803T1 (fr)
BR (1) BR0300827B1 (fr)
CA (1) CA2423745C (fr)
DE (2) DE10213788B4 (fr)
DK (1) DK1348906T3 (fr)
ES (1) ES2247432T3 (fr)
PL (1) PL200093B1 (fr)
RU (1) RU2258179C2 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102004050098B4 (de) 2004-10-14 2007-05-31 Martin GmbH für Umwelt- und Energietechnik Verbrennungsanlage, insbesondere Abfallverbrennungsanlage
DE102006026434B3 (de) 2006-06-07 2007-12-13 Forschungszentrum Karlsruhe Gmbh Verfahren zur Verbesserung der Schlackequalität von Rostfeuerungsanlagen
CN104180376B (zh) * 2014-07-18 2016-07-13 广东华信达节能环保有限公司 一种垃圾焚烧处理工艺
CN110125141A (zh) * 2019-05-14 2019-08-16 北京环境工程技术有限公司 用于垃圾焚烧飞灰熔融的床层材料及制备工艺与处理方法
CN113566210A (zh) * 2021-07-30 2021-10-29 云南紫辰集团生物科技有限公司 一种用于离心喷雾干燥的甘蔗渣焚烧热风炉
DE102021006192A1 (de) 2021-12-15 2023-06-15 Martin GmbH für Umwelt- und Energietechnik Verfahren zur Verbrennung von Abfall und Vorrichtung zur Durchführung eines derartigen Verfahrens

Citations (4)

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DE3937866A1 (de) * 1989-03-06 1990-09-13 Pauli Balduin Rostanordnung und verfahren zum verbrennen von muell und abfall
DE4404418A1 (de) * 1994-02-11 1995-08-17 Martin Umwelt & Energietech Verfahren zum Verbrennen von Brenngut, insbesondere Müll
EP0862019A1 (fr) * 1997-02-28 1998-09-02 Abb Research Ltd. Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille
EP0952391A2 (fr) * 1998-04-17 1999-10-27 Dr. Schoppe Technologie GmbH Procédé et dispositif de combustion complète des combustibles en morceaux contenant des cendres

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US2891493A (en) * 1954-09-07 1959-06-23 Babcock & Wilcox Co Method of and apparatus for burning particle-form fuel
US3745941A (en) * 1971-12-03 1973-07-17 B Reilly Slagging refuse incinerators
DE3735061A1 (de) * 1987-10-16 1989-04-27 Fischer Reinhard Verfahren zur beseitigung von abfaellen durch verbrennen mit sauerstoff
DE3929235A1 (de) * 1989-09-02 1991-03-21 Oschatz Gmbh Verfahren und vorrichtung zum beseitigen von fang- und reststoffen
DK168245B1 (da) * 1990-07-03 1994-02-28 Lund Milj Teknik A S V Fremgangsmåde og anlæg til forbrænding af fast og eventuelt flydende affald af forskellig art
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US6199492B1 (en) * 1992-02-26 2001-03-13 KüNSTLER JOHANN HANS Process for melting down combustion residues into slag
DE4301814A1 (de) * 1993-01-23 1994-07-28 Steinmueller Gmbh L & C Verfahren zum Verbrennen eines im wesentlichen aus Kunststoff bestehenden Abfalls, insbesondere PVC-Abfall
DE4429958A1 (de) * 1994-08-24 1996-02-29 Noell Abfall & Energietech Verfahren und Vorrichtung zur thermischen Behandlung von Rostschlacken
TW277101B (en) * 1995-01-21 1996-06-01 Abb Man Ag Process for treating slag from refuse incineration plants
DK90796A (da) * 1996-08-28 1998-03-01 Thomas Hoejlund Christensen Metode til udvaskning og kemisk stabilisering af flyveaske, røgrensningsprodukter og andre metalholdige materialer
EP0908674A1 (fr) * 1997-10-13 1999-04-14 Asea Brown Boveri AG Procédé pour la combustion de déchets dans un incinérateur et pour le traitement des scories provenants de l'incinération
DE19820038C2 (de) * 1998-05-05 2000-03-23 Martin Umwelt & Energietech Verfahren zum Regeln der Feuerleistung von Verbrennungsanlagen
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DE3937866A1 (de) * 1989-03-06 1990-09-13 Pauli Balduin Rostanordnung und verfahren zum verbrennen von muell und abfall
DE4404418A1 (de) * 1994-02-11 1995-08-17 Martin Umwelt & Energietech Verfahren zum Verbrennen von Brenngut, insbesondere Müll
EP0667490B1 (fr) 1994-02-11 1997-03-26 MARTIN GmbH für Umwelt- und Energietechnik Méthode pour combustion de combustible, particulièrement d'ordures ménagères
EP0862019A1 (fr) * 1997-02-28 1998-09-02 Abb Research Ltd. Procédé et dispositif pour le traitement thermique des cendres volantes des incinérateurs à grille
EP0952391A2 (fr) * 1998-04-17 1999-10-27 Dr. Schoppe Technologie GmbH Procédé et dispositif de combustion complète des combustibles en morceaux contenant des cendres

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SCHNEIDER J ET AL: "IMPROVING THE MSWI BOTTOM ASH QUALITY BY SIMPLE IN-PLANT MEASURES", ENVIRONMENTAL ASPECTS OF CONSTRUCTION WITH WASTE MATERIALS. MAASTRICHT, JUNE 1 - 3, 1994, PROCEEDINGS OF THE INTERNATIONAL CONFERENCE ON ENVIRONMENTAL IMPLICATIONS OF CONSTRUCTION WITH WASTE MATERIALS. (WASCON), AMSTERDAM, ELSEVIER, NL, vol. CONF. 2, 1 June 1994 (1994-06-01), pages 605 - 620, XP000480204 *
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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

Also Published As

Publication number Publication date
ATE301803T1 (de) 2005-08-15
BR0300827A (pt) 2004-08-17
US6748882B2 (en) 2004-06-15
RU2258179C2 (ru) 2005-08-10
CA2423745C (fr) 2008-09-09
ES2247432T3 (es) 2006-03-01
BR0300827B1 (pt) 2011-06-28
DE50300924D1 (de) 2005-09-15
US20030183138A1 (en) 2003-10-02
CA2423745A1 (fr) 2003-09-27
EP1348906B1 (fr) 2005-08-10
PL200093B1 (pl) 2008-12-31
PL359318A1 (en) 2003-10-06
DE10213788A1 (de) 2003-10-23
DK1348906T3 (da) 2005-11-07
DE10213788B4 (de) 2007-04-26
CN100352554C (zh) 2007-12-05
CN1727067A (zh) 2006-02-01

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