WO1998003250A1 - Procede de traitement des gaz brules se degageant dans une installation d'incineration de dechets organiques - Google Patents
Procede de traitement des gaz brules se degageant dans une installation d'incineration de dechets organiques Download PDFInfo
- Publication number
- WO1998003250A1 WO1998003250A1 PCT/DE1997/001515 DE9701515W WO9803250A1 WO 1998003250 A1 WO1998003250 A1 WO 1998003250A1 DE 9701515 W DE9701515 W DE 9701515W WO 9803250 A1 WO9803250 A1 WO 9803250A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- plant
- waste
- boiler
- coal
- gases
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 31
- 238000004056 waste incineration Methods 0.000 title claims abstract description 31
- 239000002912 waste gas Substances 0.000 title claims abstract description 17
- 239000010815 organic waste Substances 0.000 title description 3
- 239000003546 flue gas Substances 0.000 claims abstract description 19
- 150000001875 compounds Chemical class 0.000 claims abstract description 3
- 239000002957 persistent organic pollutant Substances 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 24
- 239000004568 cement Substances 0.000 claims description 17
- 239000003245 coal Substances 0.000 claims description 15
- 239000002699 waste material Substances 0.000 claims description 14
- 238000002485 combustion reaction Methods 0.000 claims description 12
- 238000000926 separation method Methods 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 4
- 239000003344 environmental pollutant Substances 0.000 claims description 4
- 239000002803 fossil fuel Substances 0.000 claims description 4
- 238000000227 grinding Methods 0.000 claims description 4
- 231100000719 pollutant Toxicity 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- 239000000463 material Substances 0.000 description 6
- 239000000428 dust Substances 0.000 description 5
- 150000002013 dioxins Chemical class 0.000 description 4
- 238000002309 gasification Methods 0.000 description 4
- 150000002430 hydrocarbons Chemical class 0.000 description 4
- 239000010813 municipal solid waste Substances 0.000 description 4
- 231100000331 toxic Toxicity 0.000 description 4
- 230000002588 toxic effect Effects 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 150000002240 furans Chemical class 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 230000006735 deficit Effects 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N Furan Chemical group C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000003516 soil conditioner Substances 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002023 wood 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/38—Removing components of undefined structure
- B01D53/44—Organic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/68—Halogens or halogen compounds
- B01D53/70—Organic halogen compounds
-
- 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
- F23G2201/601—Separating different calorific values
-
- 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
-
- 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
Definitions
- the invention relates to a method for the treatment of the waste gases which still occur in a waste incineration plant and which still contain organic pollutant compounds.
- the exhaust gases generated in these systems are similar to the flue gases from fossil fuels from industrial boiler systems, such as. B. coal-fired power plants, dust removal, desulfurization and mostly also subjected to denitrification.
- the object of the invention is to significantly reduce the technical and thus also the economic outlay for the separation, in particular of toxic hydrocarbon compounds, from the exhaust gases of waste incineration plants.
- This object is achieved according to the invention in a method of the type mentioned in that the exhaust gases are mixed with hot flue gases from the fossil furnace of one or more industrial boiler systems without prior separation of pollutants and are heated to a temperature> 1200 ° C.
- the mixed waste gases from the waste incineration plant can now be subjected to the usual pollutant separation (dedusting, desulphurization, denitrification) together with the flue gas from the fossil industrial boiler plant and then discharged into the atmosphere.
- pollutant separation dedusting, desulphurization, denitrification
- the heat content can now also be treated by untreated, i.e. H. Use unprepared waste directly in a cement plant.
- the waste gas produced in the waste incineration plant is expediently mixed directly with the combustion air required for the fossil combustion of the cement plant. This ensures homogeneous mixing of exhaust gas and flue gas directly behind the burner.
- the exhaust gas can also be introduced directly into the cement kiln at a corresponding point.
- the hot cooling air of the clinker cooler as combustion air for the waste incineration plant. Due to the high temperature of the clinker cooler exhaust air of approx. 800 ° C, optimal firing conditions are created in the waste incineration plant. If the waste incineration plant under reducing conditions, i.e. H. as a waste gasification plant, at least some of the heat required for gasification can also be injected from the hot flue gas of the cement kiln. In this case, the waste gas from the waste incineration plant still contains chemically bound heat, which is released by combustion in the cement kiln.
- the residues resulting from waste incineration or gasification can be carried out in the usual manner, e.g. B. for road and path construction or, in processed form, for the cement process itself as additives.
- the hot exhaust gas from the waste incineration plant can expediently also be mixed with the even hotter flue gas from a coal-fired power plant.
- the temperature level of the flue gases produced is sufficient to achieve the required minimum temperature of 1200 ° C after mixing with the waste gas from the waste incineration plant to destroy toxic ones Hydrocarbon compounds such as B. dioxins and furans.
- the waste gas from the waste incineration plant is expediently introduced into the lower region of the boiler of the coal-fired power plant, as a result of which particularly long dwell times and thus also heating times of the waste gas in the coal boiler are achieved.
- coal-fired power plants in particular, to which a waste incineration plant, so to speak, as a satellite plant, is subsequently connected, it can also make sense to mix the waste gases from the waste incineration plant directly into the combustion air for the coal burner's coal burners and to enter them into the power plant boiler.
- waste gases of the waste incineration plant into the boiler of the coal-fired power plant are discharges into the coal drop shaft of the coal mill, into the suction shaft of the smoke gas used for grinding and drying, i.e. in front of the coal mill, as well as in the presence of mill air blowers in the air duct in front of or behind the Mill air duct.
- the waste incineration plant can only be set up at a greater distance from the power plant boiler, it can also be expedient for the hot flue gases of the exhaust gases, for example in indirect or direct heat exchange with combustion air for the coal boiler , so far to cool down that a complex lining of the exhaust gas connection line between the waste incineration plant and the power plant boiler can be omitted.
- the waste intended for the waste incineration plant beforehand into a coarse fraction with a higher calorific value, which is then fed to the incineration plant, and into a fine, low calorific value fraction which is first subjected to a rotting process and then burned together with the fossil fuel in an industrial boiler, preferably a coal-fired power plant boiler.
- the high calorific value fraction is burned in a grate furnace after sorting out the largest contaminants and passing through a magnetic separation either directly or after transport with press containers. Transport in baled bales is also possible, although this requires a crushing stage.
- the flue gas from the grate furnace is fed into the coal-fired large boiler and passes through the boiler together with the flue gas from the furnace. Due to the high combustion chamber temperatures of well over 1200 ° C, pollutants are destroyed or evaporated and separated by condensation or sublimation on the fly dust in the filter or in the washer.
- the low calorific value fraction is converted into a biologically stable state in an intensive rot, whereby a rotting loss due to carbon dioxide and water vapor of about 30% arises.
- the rotting material is not pathogenic, the smell is slight, the residual moisture is 10 - 15%, landfill gas formation and leachate formation are minimized, and the material can be used for landfill construction, as a landfill cover or as a soil conditioner in certain areas.
- This material also contains approx. 30% calorific substance, which can be separated by sieving at approx. 40 ⁇ 20 mm. According to the fraction thus obtained is directly, with container or baling z. B. led to a coal-fired power plant, placed in the grinding dryer together with the design fuel and then burned in the large boiler.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP97935438A EP0912230A1 (fr) | 1996-07-18 | 1997-07-18 | Procede de traitement des gaz brules se degageant dans une installation d'incineration de dechets organiques |
AU38460/97A AU736661B2 (en) | 1996-07-18 | 1997-07-18 | Process for treating waste gases produced in an organic waste incineration plant |
Applications Claiming Priority (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19628955 | 1996-07-18 | ||
DE19628955.6 | 1996-07-18 | ||
DE19706095A DE19706095C2 (de) | 1997-02-17 | 1997-02-17 | Verfahren zur Herstellung von Zement |
DE19706095.1 | 1997-02-17 | ||
DE19707884A DE19707884A1 (de) | 1997-02-27 | 1997-02-27 | Verfahren zur Herstellung von Zement unter Verwendung von Energie aus Abfall |
DE19707884.2 | 1997-02-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998003250A1 true WO1998003250A1 (fr) | 1998-01-29 |
Family
ID=27216478
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/DE1997/001515 WO1998003250A1 (fr) | 1996-07-18 | 1997-07-18 | Procede de traitement des gaz brules se degageant dans une installation d'incineration de dechets organiques |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0912230A1 (fr) |
CN (1) | CN1128654C (fr) |
AU (1) | AU736661B2 (fr) |
WO (1) | WO1998003250A1 (fr) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2138477C1 (ru) * | 1997-11-13 | 1999-09-27 | АООТ "Кирово-Чепецкий химический комбинат им.Б.П.Константинова" | Способ очистки абгазов производства хлораля |
ES2156095A1 (es) * | 1999-12-07 | 2001-06-01 | Gil Alfredo Peris | Depurador de dioxinas y toxicos organicos volatiles de alta resistencia termica. |
WO2001059366A1 (fr) * | 2000-02-08 | 2001-08-16 | Green Island Environmental Technologies Company Limited | Methode et processus de co-combustion dans une installation de transformation de dechets en energie |
WO2015103679A1 (fr) | 2014-01-13 | 2015-07-16 | Kovachki Hristo Atanasov | Procédé pour la purification de dioxines et furanes de gaz de combustion obtenus à partir de l'incinération de déchets municipaux |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0173628A2 (fr) * | 1984-08-30 | 1986-03-05 | Christian Gérard Huret | Four pour l'incinération de déchets |
DE3504810A1 (de) * | 1985-02-13 | 1986-08-14 | Hoelter Heinz | Verfahren zur thermischen umsetzung von dioxin |
US4640681A (en) * | 1983-08-25 | 1987-02-03 | Klockner-Humboldt-Deutz Aktiengesellschaft | Method and apparatus for the removal of harmful and waste materials by combustion |
US4932335A (en) * | 1987-01-22 | 1990-06-12 | Saarbergwerke Aktiengesellschaft | Coal combustion with a fluidized incineration bed |
WO1993000982A1 (fr) * | 1991-07-12 | 1993-01-21 | Maschinen- Und Anlagenbau Grimma Gmbh | Procede et dispositif de decontamination des gaz d'echappement d'usines d'incineration de dechets |
-
1997
- 1997-07-18 AU AU38460/97A patent/AU736661B2/en not_active Ceased
- 1997-07-18 WO PCT/DE1997/001515 patent/WO1998003250A1/fr not_active Application Discontinuation
- 1997-07-18 CN CN97197954A patent/CN1128654C/zh not_active Expired - Fee Related
- 1997-07-18 EP EP97935438A patent/EP0912230A1/fr not_active Withdrawn
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4640681A (en) * | 1983-08-25 | 1987-02-03 | Klockner-Humboldt-Deutz Aktiengesellschaft | Method and apparatus for the removal of harmful and waste materials by combustion |
EP0173628A2 (fr) * | 1984-08-30 | 1986-03-05 | Christian Gérard Huret | Four pour l'incinération de déchets |
DE3504810A1 (de) * | 1985-02-13 | 1986-08-14 | Hoelter Heinz | Verfahren zur thermischen umsetzung von dioxin |
US4932335A (en) * | 1987-01-22 | 1990-06-12 | Saarbergwerke Aktiengesellschaft | Coal combustion with a fluidized incineration bed |
WO1993000982A1 (fr) * | 1991-07-12 | 1993-01-21 | Maschinen- Und Anlagenbau Grimma Gmbh | Procede et dispositif de decontamination des gaz d'echappement d'usines d'incineration de dechets |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2138477C1 (ru) * | 1997-11-13 | 1999-09-27 | АООТ "Кирово-Чепецкий химический комбинат им.Б.П.Константинова" | Способ очистки абгазов производства хлораля |
ES2156095A1 (es) * | 1999-12-07 | 2001-06-01 | Gil Alfredo Peris | Depurador de dioxinas y toxicos organicos volatiles de alta resistencia termica. |
WO2001059366A1 (fr) * | 2000-02-08 | 2001-08-16 | Green Island Environmental Technologies Company Limited | Methode et processus de co-combustion dans une installation de transformation de dechets en energie |
US7189074B2 (en) | 2000-02-08 | 2007-03-13 | Green Island Environmental Technologies Company Limited | Method and process for co-combustion in a waste to-energy facility |
WO2015103679A1 (fr) | 2014-01-13 | 2015-07-16 | Kovachki Hristo Atanasov | Procédé pour la purification de dioxines et furanes de gaz de combustion obtenus à partir de l'incinération de déchets municipaux |
Also Published As
Publication number | Publication date |
---|---|
CN1230133A (zh) | 1999-09-29 |
AU3846097A (en) | 1998-02-10 |
CN1128654C (zh) | 2003-11-26 |
EP0912230A1 (fr) | 1999-05-06 |
AU736661B2 (en) | 2001-08-02 |
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