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DE10027200A1 - Process for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants, especially lignite-fired power plants with wet flue gas desulfurization - Google Patents

Process for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants, especially lignite-fired power plants with wet flue gas desulfurization

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Publication number
DE10027200A1
DE10027200A1 DE10027200A DE10027200A DE10027200A1 DE 10027200 A1 DE10027200 A1 DE 10027200A1 DE 10027200 A DE10027200 A DE 10027200A DE 10027200 A DE10027200 A DE 10027200A DE 10027200 A1 DE10027200 A1 DE 10027200A1
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DE
Germany
Prior art keywords
water
power plants
fired power
coke
waste
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Withdrawn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
DE10027200A
Other languages
German (de)
Inventor
Ralf Peter
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.)
VEAG Vereinigte Energiewerke AG
Original Assignee
VEAG Vereinigte Energiewerke AG
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
Priority claimed from DE19925011A external-priority patent/DE19925011C2/en
Application filed by VEAG Vereinigte Energiewerke AG filed Critical VEAG Vereinigte Energiewerke AG
Priority to DE10027200A priority Critical patent/DE10027200A1/en
Priority to PCT/EP2000/004743 priority patent/WO2000071934A1/en
Publication of DE10027200A1 publication Critical patent/DE10027200A1/en
Withdrawn legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0273Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using indirect heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/006General arrangement of incineration plant, e.g. flow sheets
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/08Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
    • F23G5/14Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
    • F23G5/16Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/442Waste feed arrangements
    • F23G5/444Waste feed arrangements for solid waste
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/46Recuperation of heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/70Blending
    • F23G2201/701Blending with additives
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00Combustion
    • F23G2202/10Combustion in two or more stages
    • F23G2202/102Combustion in two or more stages with supplementary heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00Waste heat recuperation
    • F23G2206/20Waste heat recuperation using the heat in association with another installation
    • F23G2206/201Waste heat recuperation using the heat in association with another installation with an industrial furnace
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00Waste heat recuperation
    • F23G2206/20Waste heat recuperation using the heat in association with another installation
    • F23G2206/203Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/00001Exhaust gas recirculation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/50206Pelletising waste before combustion
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

Die Erfindung betrifft ein Verfahren nach 19925011.1-13 zur thermischen Entsorgung von heizwertreichen Fraktionen aus sortiertem Müll und/oder Reststoff in fossil gefeuerten Kraftwerksanlagen, insbesondere Braunkohlekraftwerken mit nasser Rauchgasentschwefelung. DOLLAR A Der Erfindung liegt die Aufgabe zugrunde, den bei der Pyrolyse entstehenden Koks teilweise bzw. vollständig von Schadstoffen, insbesondere von Chlor, zu befreien und die dabei entstehenden Abprodukte rückstandsfrei und umweltfreundlich zu verbringen. DOLLAR A Dies wird erfindungsgemäß dadurch erreicht, daß der bei der Pyrolyse aus Müll und/oder Reststoff entstehende Koks in einem Wäscher, insbesondere in einem einstufigen und/oder mehrstufigen mit Umgebungstemperatur temperierten Wasser und/oder Brauchwasser eines Wasserbades und/oder eines Tauchbades und/oder eines Düsenbades von Schadstoffen, speziell von Chlor, im Anteil von >= 50% befreit und anschließend der chlorreduzierte Koks einem konventionellen Verbrennungsprozeß eines nachgeschalteten Dampferzeugers zugeführt wird und das im Wäscher entstehende mit ca. 100 g/l Chlorid versetzte Waschwasser dem im Kraftwerksprozeß anfallenden Rauchgasentschwefelungswasser in einer Menge von ca. 5% bis ca. 10% zugesetzt wird und gemeinsam mit der Dampfkesselasche als Stabilisat auf der Deponie verbracht wird.The invention relates to a method according to 19925011.1-13 for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants, in particular lignite-fired power plants with wet flue gas desulfurization. DOLLAR A The object of the invention is to partially or completely free the coke formed in the pyrolysis of pollutants, in particular chlorine, and to dispose of the resulting waste products in a residue-free and environmentally friendly manner. DOLLAR A This is achieved according to the invention in that the coke formed in the pyrolysis from waste and / or residual material in a scrubber, in particular in a single-stage and / or multi-stage water and / or process water of a water bath and / or an immersion bath and / or or a jet bath freed of pollutants, especially chlorine, in a proportion of> = 50% and then the chlorine-reduced coke is fed to a conventional combustion process of a downstream steam generator and the washing water which is created in the scrubber and contains about 100 g / l of chloride is added to the water generated in the power plant process Flue gas desulfurization water is added in an amount of approx. 5% to approx. 10% and spent together with the steam ash as a stabilizer on the landfill.

Description

Die Erfindung betrifft ein Verfahren nach der DE 199 25 011 zur thermischen Entsorgung von heizwertreichen Fraktionen aus sortiertem Müll und/oder Rest­ stoff in fossil gefeuerten Kraftwerksanlagen, insbesondere Braunkohlekraftwer­ ken mit nasser Rauchgasentschwefelung.The invention relates to a method according to DE 199 25 011 for thermal Disposal of high calorific fractions from sorted waste and / or rest substance in fossil-fired power plants, especially lignite-fired power plants with wet flue gas desulfurization.

Nach der DE 199 25 011 ist zur thermischen Entsorgung von heizwertreichen Fraktionen ein Verfahren bekannt, bei dem sortierter Müll und/oder Reststoffe in fossil gefeuerten Kraftwerksanlagen, insbesondere in Kohlekraftwerken mit nasser Rauchgasentschwefelungsanlage, verbracht wird. Dazu ist der behan­ delte und aufbereitete Müll/Reststoff in an sich bekannten Pellets bzw. Briketts gepreßt oder einer thermischen Behandlung (Pyrolyse) zur Bildung von koksar­ tigem Material und energiereichem Gas unterzogen und ggf. gesteuert in Ab­ hängigkeit von jeweils notwendigen Gas- und Koksanalysen sowie der Gas- und Koksmengen mit Additiven versetzt sowie dem Kohlestrom im Entladebunker und/oder einem Kohlebunker und/oder einem Dampferzeugerbunker und/oder einem Kohlezuteiler vor oder im Bereich eines Kohlefallschachtes und/oder ei­ ner Rauchgasrücksaugung in einem Anteil von max. 5% der Zuteilerkohlemen­ ge ab vorzugsweise 60% Feuerungsleistung des Kessels direkt zugegeben.According to DE 199 25 011 is for thermal disposal of high calorific value Fractions known a process in which sorted waste and / or residues in fossil-fired power plants, especially in coal-fired power plants wet flue gas desulfurization plant, is spent. The behan is Deleted and processed waste / residual material in pellets or briquettes known per se pressed or a thermal treatment (pyrolysis) to form koksar material and energy-rich gas and, if necessary, controlled in Ab dependence on the necessary gas and coke analyzes as well as the gas and Amounts of coke with additives and the coal stream in the unloading bunker and / or a coal bunker and / or a steam generator bunker and / or a coal distributor in front of or in the area of a coal chute and / or egg ner smoke evacuation in a proportion of max. 5% of the allot coal ge preferably added from preferably 60% firing capacity of the boiler.

Weiterhin wird der aufbereitete und behandelte Müll/Reststoff einer Kohlemühle zugeführt und im Dampferzeuger verbrannt, wobei das bei der thermischen Be­ handlung entstandene energiereiche Gas teilweise oder vollständig auf direk­ tem Wege dem Dampferzeuger zugeführt und unter teilweisem oder vollständi­ gem Verzicht auf eine separate Reinigung verbrannt wird.Furthermore, the processed and treated waste / residue from a coal mill fed and burned in the steam generator, which in the thermal loading energy generated gas partially or completely on direct supplied to the steam generator and partially or completely is burned without a separate cleaning.

Nachteiligerweise fällt während des Prozesses der Pyrolyse Koks an, der mit Schadstoffen, insbesondere mit Chlor, versetzt ist.Disadvantageously, during the pyrolysis process, coke is produced Pollutants, especially with chlorine, is added.

Der Erfindung liegt die Aufgabe zugrunde, den bei der Pyrolyse entstehenden Koks teilweise bzw. vollständig von Schadstoffen, insbesondere von Chlor, zu befreien und die dabei entstehenden Abprodukte rückstandsfrei und umwelt­ freundlich zu verbringen.The invention has for its object the resulting during pyrolysis Coke partially or completely from pollutants, especially chlorine liberate and the resulting waste products free of residues and the environment to spend friendly.

Dies wird erfindungsgemäß dadurch erreicht, daß der bei der Pyrolyse aus Müll und/oder Reststoff entstehende Koks in einem Wäscher, insbesondere in einem einstufigen und/oder mehrstufigen mit Umgebungstemperatur temperierten Wasser und/oder Brauchwasser eines Wasserbades und/oder eines Tauchba­ des und/oder eines Düsenbades von Schadstoffen, speziell von Chlor, im Anteil von ≧ 50% befreit und anschließend der chlorreduzierte Koks einem konven­ tionellen Verbrennungsprozeß eines nachgeschalteten Dampferzeugers zuge­ führt wird.This is achieved according to the invention in that the pyrolysis from garbage and / or coke produced in a scrubber, in particular in a single-stage and / or multi-stage tempered with ambient temperature Water and / or process water from a water bath and / or a diving pool  of and / or a jet bath of pollutants, especially chlorine, in the proportion freed from ≧ 50% and then the chlorine-reduced coke to a con tional combustion process of a downstream steam generator leads.

An einem Ausführungsbeispiel soll nachfolgend die Erfindung näher erläutert werden. Die dazugehörige Zeichnung zeigt das Schema der Verfahrensweise zur Schadstoffbeseitigung von Chlor aus Koks.The invention is explained in more detail below using an exemplary embodiment become. The accompanying drawing shows the scheme of the procedure for removing chlorine from coke.

Beim Verfahren zur thermischen Entsorgung von heizwertreichen Fraktionen mit hohem bis niedrigem Heizwert wird aufbereiteter und/oder vorbehandelter und/oder unbehandelter und/oder sortierter und/oder unsortierter Müll 1 und/oder Reststoff entweder in Containern zwischenverpreßt oder als Pellets und/oder als Briketts verpreßt und/oder in loser Form mit einer Kantenlänge von max. ≦ 200 mm in fossil gefeuerten Kraftwerksanlagen verbrannt. Insbe­ sondere handelt es sich um Kohlekraftwerke mit einer nassen Rauchgasent­ schwefelungsanlage. Die thermische Behandlung des Mülls 1 und/oder Rest­ stoffes wird über eine Pyrolyse 2 realisiert. Dabei wird der Müll 1 und/oder Reststoff mit einer max. Kantenlänge von 200 mm pro Stück in der größten Ausdehnung einer thermischen Behandlung (Homogenisierung) in Form einer Pyrolyse 2 mit einem Pyrolyse-Rohr als Vorschaltanlage vor einer fossil gefeu­ erten Kraftwerksanlage unterzogen. Beim Prozeß der Pyrolyse 2 des Mülls 1 und/oder Reststoffes entstehen Koks 3 und energiereiches Gas. Der Koks 3 wird in einem einstufigen und/oder mehrstufigen Wäscher 42, wobei das Was­ ser und/oder Brauchwasser Umgebungstemperatur aufweist, in einem Wasser­ bad und/oder Tauchbad und/oder Düsenbad von Schadstoffen, speziell von Chlor, im Anteil von ≧ 50% befreit. Anschließend wird der von Chlor befreite Koks 5 gemeinsam mit dem energiereichen Gas und mit Kohle in einem kon­ ventionellen Verbrennungsprozeß einem nachgeschalteten Dampferzeuger 9 zugeführt.In the process for the thermal disposal of high-calorific value fractions with a high to low calorific value, processed and / or pretreated and / or untreated and / or sorted and / or unsorted waste 1 and / or residual material is either pressed in containers or pressed as pellets and / or as briquettes and / or in bulk with an edge length of max. ≦ 200 mm burned in fossil-fired power plants. In particular, it concerns coal-fired power plants with a wet flue gas desulphurization plant. The thermal treatment of the waste 1 and / or residual material is realized via pyrolysis 2 . The garbage 1 and / or residual material with a max. Edge length of 200 mm per piece in the largest extent subjected to thermal treatment (homogenization) in the form of pyrolysis 2 with a pyrolysis tube as a ballast in front of a fossil-fired power plant. In the process of pyrolysis 2 of waste 1 and / or residual material, coke 3 and high-energy gas are produced. The coke 3 is in a one-stage and / or multi-stage scrubber 42 , the water and / or process water being at ambient temperature, in a water bath and / or immersion bath and / or jet bath of pollutants, especially chlorine, in a proportion of ≧ 50% exempted. Then the chlorine-free coke 5 is fed to a downstream steam generator 9 together with the high-energy gas and coal in a conventional combustion process.

Durch zusätzliche intensive Versuche wurde dabei herausgefunden, daß bei einem wesentlich höherem Chloreintrag des Mülls 1 und/oder Reststoffes ge­ genüber der Kohle die Chlorfraktion des Gas/Koksgemisches von ≦ 40 kg HCl/h einzuhalten ist, um negative Korrosionsfolgen in den Anlagen zu vermei­ den. Through additional intensive tests it was found that the chlorine fraction of the gas / coke mixture of ≦ 40 kg HCl / h is to be observed with a significantly higher chlorine input of waste 1 and / or residual material compared to coal, in order to avoid the negative consequences of corrosion in the plants .

Das im Wäscher 4 entstehende mit ca. ≦ 100 g/l Chlorid versetzte Waschwas­ ser 6 wird dem im Kraftwerksprozeß üblicherweise anfallenden Rauchgasent­ schwefelungswasser 7 in einer Menge von ca. ≦ 5% bis ca. ≦ 10% zugesetzt, und zusammen mit der Dampfkesselasche 8 als Stabilisat 10 auf einer Deponie verbracht.The resulting in the washer 4 with about ≦ 100 g / l chloride offset Waschwas ser 6 the commonly encountered in the power plant process Rauchgasent is desulphurisation water 7 is added in an amount of about ≦ 5% to about ≦ 10%, and together with the boiler ash 8 spent as Stabilisat 10 on a landfill.

Durch die Erfindung werden folgende Vorteile erzielt:
The following advantages are achieved by the invention:

  • - umweltfreundliche Verbringung der beim Prozeß entstehenden Abprodukte durch rückstandsfreie Beseitigung im vorhandenen Kraftwerksprozeß- Environmentally friendly shipment of the waste products resulting from the process through residue-free disposal in the existing power plant process
  • - weitestgehende Befreiung des bei der Pyrolyse entstehenden Kokses von Schadstoffen, insbesondere von Chlor- The coke produced during pyrolysis is largely exempt from Pollutants, especially chlorine
  • - Verwendung des beim Waschprozeß entstehenden Waschwassers als Sta­ bilisat bei der Verbringung der Dampfkesselasche auf die Deponie- Use of the washing water created during the washing process as Sta bilisat when the boiler ash is brought to the landfill
Aufstellung der verwendeten BezugszeichenList of the reference symbols used

11

Müll
rubbish

22

Pyrolyse
Pyrolysis

33rd

Koks
coke

44

Wäscher
washer

55

Koks
coke

66

Waschwasser
Wash water

77

Rauchgasentschwefelungswasser
Flue gas desulfurization water

88th

Dampfkesselasche
Boiler ash

99

Dampferzeuger
Steam generator

1010th

Stabilisat
Stabilize

Claims (3)

1. Verfahren nach der DE 199 25 011 zur thermischen Entsorgung von heiz­ wertreichen Fraktionen aus sortiertem Müll und/oder Reststoff in fossil gefeu­ erten Kraftwerksanlagen, insbesondere Kohlekraftwerken mit nasser Rauchgas­ entschwefelung, bei dem der Müll/Reststoffe aufbereitet und behandelt und zu an sich bekannten Pellets/Briketts gepreßt oder einer thermischen Behandlung (Pyrolyse) zur Bildung von koksartigem Material und energiereichem Gas un­ terzogen und ggf. gesteuert in Abhängigkeit von jeweils notwendigen Gas- und Koksanalysen sowie der Gas- und Koksmengen mit Additiven versetzt, dem Kohlestrom im Entladebunker und/oder einem Kohleband und/oder einem Dampferzeugerbunker und/oder einem Kohlezuteiler vor oder im Bereich eines Kohlefallschachtes und/oder einer Rauchgasrücksaugung in einem Anteil von max. 5% der Zuteiler-Kohlemenge ab vorzugsweise 60% Feuerungsleistung des Kessels direkt aufgegeben, zusammen einer Kohlemühle zugeführt sowie im Dampferzeuger verbrannt wird, wobei das bei der thermischen Behandlung entstandene energiereiche Gas teilweise oder vollständig auf direktem Wege dem Dampferzeuger zugeführt und unter teilweisem oder vollständigem Ver­ zicht auf eine separate Reinigung verbrannt wird, gekennzeichnet dadurch, daß der bei der Pyrolyse aus Müll und/oder Reststoff entstehende Koks in ei­ nem Wäscher, insbesondere in einem einstufigen und/oder mehrstufigen mit Umgebungstemperatur temperierten Wasser und/oder Brauchwasser eines Wasserbades und/oder eines Tauchbades und/oder eines Düsenbades von Schadstoffen, speziell von Chlor, im Anteil von ≧ 50% befreit und anschließend der chlorreduzierte Koks einem konventionellen Verbrennungsprozeß eines nachgeschalteten Dampferzeugers zugeführt wird.1. The method according to DE 199 25 011 for the thermal disposal of high-value fractions from sorted waste and / or residual material in fossil-fired power plants, in particular coal-fired power plants with wet flue gas desulfurization, in which the waste / residual materials are processed and treated and known Pressed pellets / briquettes or subjected to thermal treatment (pyrolysis) to form coke-like material and high-energy gas and, if necessary, controlled with additives, the coal stream in the unloading bunker and / or controlled depending on the gas and coke analyzes required as well as the gas and coke quantities. or a coal belt and / or a steam generator bunker and / or a coal distributor in front of or in the area of a coal chute and / or a flue gas recirculation in a proportion of max. 5% of the feeder coal quantity, preferably from 60% firing capacity of the boiler, is given up directly, fed together to a coal mill and burned in the steam generator, the energy-rich gas produced during the thermal treatment being supplied to the steam generator partly or completely directly and with partial or complete Ver Zicht is burned to a separate cleaning, characterized in that the coke formed during the pyrolysis of waste and / or residual material in a scrubber, in particular in a one-stage and / or multi-stage water and / or process water of a water bath and / or at ambient temperature an immersion bath and / or a nozzle bath is freed of pollutants, especially chlorine, in a proportion of ≧ 50% and then the chlorine-reduced coke is fed to a conventional combustion process of a downstream steam generator. 2. Verfahren nach Anspruch 1, gekennzeichnet dadurch, daß das im Wäscher entstehende mit ca. ≦ 100 g/l Chlorid versetzte Waschwasser dem im Kraft­ werksprozeß anfallenden Rauchgasentschwefelungswasser in einer Menge von ca. ≦ 5% bis ca. ≦ 10% zugesetzt wird und gemeinsam mit der Dampfkessel­ asche als Stabilisat auf der Deponie verbracht wird. 2. The method according to claim 1, characterized in that in the washer resulting wash water with approx. g 100 g / l chloride added to the in the power flue gas desulfurization water in an amount of approx. ≦ 5% to approx. ≦ 10% is added and together with the steam boiler ash is brought to the landfill as a stabilizer.   3. Verfahren nach Anspruch 1, gekennzeichnet dadurch, daß unbehandelter Müll/Reststoff mit hohem bis niedrigem Heizwert unsortiert in loser Form mit einer Kantenlänge von max. 200 mm pro Müllstück und/oder pro Reststoff der Pyrolyse unterzogen wird.3. The method according to claim 1, characterized in that untreated Garbage / residue with high to low calorific value unsorted in loose form an edge length of max. 200 mm per piece of waste and / or per residue Undergoes pyrolysis.
DE10027200A 1999-05-25 2000-05-23 Process for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants, especially lignite-fired power plants with wet flue gas desulfurization Withdrawn DE10027200A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
DE10027200A DE10027200A1 (en) 1999-05-25 2000-05-23 Process for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants, especially lignite-fired power plants with wet flue gas desulfurization
PCT/EP2000/004743 WO2000071934A1 (en) 1999-05-25 2000-05-23 Method for thermally disposing of fractions having a high calorific value and contained in refuse in fossil-fired power plants

Applications Claiming Priority (2)

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DE19925011A DE19925011C2 (en) 1999-05-25 1999-05-25 Process for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants
DE10027200A DE10027200A1 (en) 1999-05-25 2000-05-23 Process for the thermal disposal of high-calorific fractions from sorted waste and / or residues in fossil-fired power plants, especially lignite-fired power plants with wet flue gas desulfurization

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DE10027200A1 true DE10027200A1 (en) 2001-11-29

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CA2418601A1 (en) 2002-03-25 2003-09-25 Industrial Energy Management Solutions, Inc. Gasification system
EP1498659A1 (en) * 2003-07-17 2005-01-19 Industrial Energy Management Solutions, Inc. Gasification system
DE102004002388A1 (en) * 2004-01-15 2005-08-11 Swb Erzeugung Gmbh & Co.Kg, Process for the energetic use of alternative fuels, pyrolysis plant for substitute fuels as well as combination of pyrolysis plant and combustion plant for the combustion of pyrolysis gases
AT514400B1 (en) * 2013-05-31 2015-05-15 Cleanstgas Gmbh Plant for gasifying lumpy fuels
CN104593026B (en) * 2015-01-28 2017-06-09 中国重型机械研究院股份公司 A kind of scale low order fine coal low temperature pyrogenation device and method

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GB1562492A (en) * 1976-08-02 1980-03-12 Foster Wheeler Power Prod Pyrolysis of waste
DE3044991A1 (en) 1980-11-28 1982-07-01 Steag Ag, 4300 Essen Coal plus refuse burning power station - has refuse-fired boiler steam fed into coal-fired boiler system after high-pressure turbine, before reheater
DE3428782A1 (en) * 1984-08-04 1986-02-13 Metallgesellschaft Ag, 6000 Frankfurt METHOD FOR PRODUCING IRON SPONGE
DE3811820A1 (en) 1987-08-03 1989-02-16 Siemens Ag METHOD AND SYSTEM FOR THERMAL WASTE DISPOSAL
DE4011706A1 (en) 1990-04-11 1991-10-24 Hoelter Heinz Fuel prepn. from waste and coal - by freeing waste from substances causing harmful emissions and mixing with very fine
DE4126838C2 (en) 1991-08-14 1994-06-09 Hoelter Heinz Waste disposal procedures
US5471937A (en) * 1994-08-03 1995-12-05 Mei Corporation System and method for the treatment of hazardous waste material
DE19538736A1 (en) * 1994-11-03 1996-05-09 Volkswagen Ag Pre-carbonisation before direct waste incineration for reduced costs etc.
DE4440984C2 (en) 1994-11-17 1997-08-21 Siemens Ag Power plant with a gas turbine
DE4442136C2 (en) 1994-11-26 1997-10-02 Hoelter Heinz Process for the combustion of fossil fuel and waste
DE19510390A1 (en) * 1995-03-22 1996-09-26 Siemens Ag Carbonising waste to form e.g. pyrolysis prod.
FR2762613B1 (en) * 1997-04-25 1999-06-11 Traidec Sa PLANT FOR THERMOLYSIS TREATMENT AND FOR ENERGY RECOVERY OF WASTE

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