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 desulfurizationInfo
- 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
- Authority
- 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- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims abstract description 19
- 239000002699 waste material Substances 0.000 title claims abstract description 18
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 10
- 239000003546 flue gas Substances 0.000 title claims abstract description 10
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 8
- 230000023556 desulfurization Effects 0.000 title claims abstract description 8
- 239000000571 coke Substances 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 238000000197 pyrolysis Methods 0.000 claims abstract description 15
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims abstract description 14
- 229910052801 chlorine Inorganic materials 0.000 claims abstract description 14
- 239000000460 chlorine Substances 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 12
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 8
- 231100000719 pollutant Toxicity 0.000 claims abstract description 8
- 238000002485 combustion reaction Methods 0.000 claims abstract description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims abstract description 3
- 238000007654 immersion Methods 0.000 claims abstract description 3
- 239000003381 stabilizer Substances 0.000 claims abstract 2
- 239000003245 coal Substances 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 11
- 238000007669 thermal treatment Methods 0.000 claims description 5
- 239000010813 municipal solid waste Substances 0.000 claims description 4
- 239000008188 pellet Substances 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 claims description 2
- 238000010304 firing Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 abstract description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 230000009189 diving Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
- F23G5/0273—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using indirect heating
-
- 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
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
-
- 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
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
-
- 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
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/70—Blending
- F23G2201/701—Blending with additives
-
- 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
- F23G2202/102—Combustion in two or more stages with supplementary heating
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/201—Waste heat recuperation using the heat in association with another installation with an industrial furnace
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
-
- 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
- F23G2900/00001—Exhaust gas recirculation
-
- 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
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/30—Technologies 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
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)
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)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| 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 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE10027200A1 true DE10027200A1 (en) | 2001-11-29 |
Family
ID=26005925
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE10027200A Withdrawn 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 |
Country Status (2)
| Country | Link |
|---|---|
| DE (1) | DE10027200A1 (en) |
| WO (1) | WO2000071934A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
-
2000
- 2000-05-23 WO PCT/EP2000/004743 patent/WO2000071934A1/en not_active Ceased
- 2000-05-23 DE DE10027200A patent/DE10027200A1/en not_active Withdrawn
Also Published As
| Publication number | Publication date |
|---|---|
| WO2000071934A1 (en) | 2000-11-30 |
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