EP0850289B1 - Procede et dispositif permettant de produire du gaz combustible - Google Patents
Procede et dispositif permettant de produire du gaz combustible Download PDFInfo
- Publication number
- EP0850289B1 EP0850289B1 EP96942977A EP96942977A EP0850289B1 EP 0850289 B1 EP0850289 B1 EP 0850289B1 EP 96942977 A EP96942977 A EP 96942977A EP 96942977 A EP96942977 A EP 96942977A EP 0850289 B1 EP0850289 B1 EP 0850289B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- gasification
- grate
- medium
- regulated
- fuel gas
- 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.)
- Expired - Lifetime
Links
- 239000002737 fuel gas Substances 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 11
- 238000002309 gasification Methods 0.000 claims abstract description 80
- 239000007789 gas Substances 0.000 claims abstract description 20
- 238000001816 cooling Methods 0.000 claims abstract description 14
- 230000001105 regulatory effect Effects 0.000 claims abstract description 13
- 239000002699 waste material Substances 0.000 claims abstract description 9
- 230000001143 conditioned effect Effects 0.000 claims abstract description 6
- 238000002485 combustion reaction Methods 0.000 claims description 19
- 239000007787 solid Substances 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 238000009413 insulation Methods 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 abstract description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 7
- 229910052799 carbon Inorganic materials 0.000 abstract description 7
- 239000000571 coke Substances 0.000 abstract description 3
- 239000002826 coolant Substances 0.000 abstract 1
- 230000005611 electricity Effects 0.000 abstract 1
- 239000012212 insulator Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 5
- 238000005192 partition Methods 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 230000005526 G1 to G0 transition Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/80—Other features with arrangements for preheating the blast or the water vapour
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/22—Arrangements or dispositions of valves or flues
- C10J3/24—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/22—Arrangements or dispositions of valves or flues
- C10J3/24—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed
- C10J3/26—Arrangements or dispositions of valves or flues to permit flow of gases or vapours other than upwardly through the fuel bed downwardly
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/32—Devices for distributing fuel evenly over the bed or for stirring up the fuel bed
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
- C10J3/34—Grates; Mechanical ash-removing devices
- C10J3/36—Fixed grates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/723—Controlling or regulating the gasification process
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/74—Construction of shells or jackets
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/86—Other features combined with waste-heat boilers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/02—Dust removal
- C10K1/024—Dust removal by filtration
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1603—Integration of gasification processes with another plant or parts within the plant with gas treatment
- C10J2300/1606—Combustion processes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1671—Integration of gasification processes with another plant or parts within the plant with the production of electricity
Definitions
- the invention relates to a method and a device for the production of fuel gas from carbonaceous Products, especially those suitably conditioned or processed waste and residues.
- DE-OS 33 12 863 is a method for burning of combustible material in the combustible exhaust gases of a combustion chamber be fed, known.
- DE-PS 34 09 292 and DE-PS 37 05 406 are Gas generator in a unit with a combustion chamber as a so-called Gasification boiler known. These consist of one arranged above a movable grate Filling shaft, one at the filling shaft above the Grate subsequent reaction space, one below the Grate arranged combustion chamber and one inside the Combustion chamber provided flame tube.
- DE-PS 926 978 specifies a gas generator in which the Gasification of the fuel in a cross-flow of the gasification agent he follows.
- the front wall of the gasification duct is designed as an inclined grate, the superimposed, individually switchable wind chambers are upstream. This can be switched off wind chambers optionally, the combustion agent according to need Air or air and steam are fed, causing the combustion process can be influenced.
- the invention has for its object a method and to create a device with which one high energy efficiency the purity of the in one Gasification apparatus generated gas and thus its Usability is expanded.
- a largely full utilization of the used in the Waste or residual carbon one optimal usability of the fuel gas generated and a minimization of the pollutant discharge by which combustion exhaust gases escaping heat become.
- the invention solves the problem for the method with the characterizing means of claim 1 and for Device with the characterizing means of the claim 2.
- Advantageous embodiments of the device Claim 2 are characterized in the subclaims 3 and 4.
- the suitably conditioned or prepared Waste or residues are called solids with air or an air or oxygen-containing gas mixture as Gasifying agent gasified in a gasifying apparatus.
- the substance to be gasified and the gasifying agent in the Mixed flow led by the solid to be gasified passes through the gasification furnace from top to bottom and that Gasifying agents both from above and from below and sideways, at least sideways and on one of the others mentioned places, the solid bed is fed and the extraction of the fuel gas preferably at the lateral supply of the gasification agent opposite Side is done.
- the regulation of the gasification process in the gasification apparatus takes place according to the invention by recording the temperature profile about the height of the gasification apparatus. Doing so the vertical position of the main gasification zone, accordingly the maximum temperature zone, via the movement of the sliding grate and thus the speed of the ash discharge regulated.
- different optimal gasification temperature is about Size and composition of the gasification gas flow and the performance of the gasification furnace across the width of the Gasification agent supply through one above the other Feed points regulated.
- the fuel gas generated can be completely or partially without further processing one under the gasifier in Unit arranged combustion chamber known per se Type supplied and the resulting combustion gases be used thermally.
- the residual heat is by means of a Heat recovery boiler used thermally. After heat removal the combustion exhaust gas is subjected to flue gas cleaning, which preferably contains an activated coke filter, and then gets into the via a chimney The atmosphere.
- the device for the production of fuel gas by gasification carbon-containing products, especially suitable ones Way conditioned and prepared waste and Residues, with air or with air or oxygen Gas mixture as a gasifying agent in one Gasification apparatus, preferably in a unit with one Combustion chamber, is characterized in that the gasifier equipped with a sloping grate is, which is preferably designed as a step grate, the enables the supply of the gasification agent and over a suitable mechanism in a pushing movement is.
- the device the gasifier, surrounded by a two-layer insulation-cooling system, its layers through a perforated partition are separated, the outer insulating layer one or several openings for the cooling air inlet and the inner cooling layer one or more openings for the Have cooling air discharge.
- the cold cooling gas flow usually the gasifying agent
- the outer wall of the insulated cooling system cools, then the flowed through perforated partition and thus in the Follow also on the inner mantle of the gasifier is blown. This leads to intensive cooling the inner shell of the gasifier simultaneous advantageous preheating of the gasification agent.
- the gasifier has a sloping grate 1 equipped, with part of the gasification agent to the gasifying substance is fed through this grate 1 and mainly does the job in the insert bag fully implement any carbon still present.
- Another portion of gasification agent is the gasification furnace fed above the solid bed and has mainly the task of smoldering products of the gasified Flush substance into the gasification zone and thus the complete gasification.
- the bulk of the Gasification agent is laterally over the gasification apparatus a feeder 2 supplied. By varying the width of the Lateral gas supply can be the dimension the gasification zone and thus the gasification performance become.
- the inclined grate 1 is a stepped grate or otherwise than deviating from a flat shape trained and movably mounted as a sliding grate.
- a suitable drive 4 By the thrust movement via a suitable drive 4 is the Ash is discharged through a discharge opening 5 and arrives into the ash collecting area 6.
- the fuel gas is largely removed from the fuel gas and ash free of carbon-containing and mineral suspended particles.
- Another feature of the invention is the insulated cooling system around the gasifier.
- the cooling air arrives first in an outer insulating layer 7 and from there through the perforated partition 8 into an inner cooling layer 9, where the actual cooling of the gasification furnace jacket 12 takes place.
- the preheated air leaves it Insulating cooling system with a 10 outlet and is called Gasification agent or combustion air used.
- the regulation of the gasification process in the gasification apparatus takes place, as already described, by inclusion of the Temperature profile over the height of the gasifier.
- the location of the main gasification zone becomes corresponding the maximum temperature zone, via the movement of the grate 1 and thus regulated by the ash discharge.
- different optimal Gasification temperature is about size and composition of the gasification medium flow and the performance of the gasification apparatus accordingly across the width of the gasification zone the width of the gasifier feed several feeders 2 arranged one above the other are regulated.
- the fuel gas generated can be completely or partially without further processing one under the gasifier in Unit arranged combustion chamber 11 known per se Type supplied and the resulting combustion gases be used thermally.
- the residual heat is by means of a Heat recovery boiler used thermally. After heat removal the combustion exhaust gas is subjected to flue gas cleaning, preferably using an activated coke filter, and then enters via a chimney the atmosphere.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Gasification And Melting Of Waste (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Industrial Gases (AREA)
- Manufacture, Treatment Of Glass Fibers (AREA)
- Carbon And Carbon Compounds (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Incineration Of Waste (AREA)
Claims (4)
- Procédé pour la régulation de la fabrication d'un gaz combustible à partir de matières solides carbonées, en particulier de déchets et de résidus, qui sont conditionnés, respectivement préparés de façon appropriée, par gazéification avec un agent de gazéification, se composant d'air ou d'un mélange gazeux contenant de l'oxygène, dans un appareil de gazéification, dans lequel les matières solides à gazéifier traversent l'appareil de gazéification de haut en bas et la gazéification a lieu dans la masse des matières solides à gazéifier dans une zone de gazéification située au-dessus d'une grille et l'agent de gazéification est introduit en un courant mixte dans la zone de gazéification par le bas à travers la grille et/ou par le haut ainsi que latéralement et l'extraction du gaz combustible hors de l'appareil de gazéification est effectuée par le côté opposé à l'introduction latérale de l'agent de gazéification, dans lequel le courant principal de l'agent de gazéification est introduit latéralement dans la zone de gazéification, et la régulation de l'opération de gazéification est effectuée en fonction du profil de température enregistré dans la masse, caractérisé en ce que la situation de la zone de gazéification principale est régulée par la vitesse de l'extraction des cendres hors de l'appareil de gazéification, la température optimale de gazéification par le courant d'agent de gazéification et la puissance de l'appareil de gazéification par le réglage de la largeur de la zone de gazéification au moyen de l'introduction latérale de l'agent de gazéification.
- Dispositif pour la fabrication d'un gaz combustible à partir de matières solides carbonées, en particulier de déchets et de résidus, qui sont conditionnés, respectivement préparés de façon appropriée, dans lequel les matières solides à gazéifier traversent un appareil de gazéification de haut en bas et la gazéification a lieu dans la masse des matières solides à gazéifier essentiellement au-dessus d'une grille, il existe des moyens qui introduisent l'agent de gazéification en un courant mixte par le bas à travers la grille et/ou par le haut ainsi que latéralement et qui l'extraient par le côté opposé à l'introduction latérale, caractérisé en ce que l'appareil de gazéification présente une grille oblique (1), qui est équipée d'un mécanisme, qui peut mouvoir la grille en un mouvement de translation, de telle façon que l'extraction des cendres puisse être régulée.
- Dispositif suivant la revendication 2, caractérisé en ce que la grille oblique (1) est une grille à étages.
- Dispositif suivant l'une des revendications 2 ou 3, caractérisé en ce que la paroi extérieure de l'appareil de gazéification présente une isolation thermique composée d'un système de refroidissement et d'isolation à deux couches, dont les couches individuelles sont séparées l'une de l'autre par une paroi intermédiaire perforée (8), dans lequel il existe des moyens par lesquels un agent de combustion froid peut être introduit dans la couche extérieure, qui est la couche isolante (7), être introduit ensuite par la paroi intermédiaire perforée (8) dans la couche intérieure, qui est la couche de refroidissement (9), être extrait hors de la couche intérieure sous forme d'agent de combustion chauffé et être fourni à l'appareil de gazéification au moins par 1' (les) introduction(s) latérale(s) (2).
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE8100006 | 1995-06-27 | ||
PCT/DE1995/000816 WO1997001617A1 (fr) | 1995-06-27 | 1995-06-27 | Procede et dispositif permettant de produire du gaz combustible |
PCT/DE1996/001122 WO1997001618A1 (fr) | 1995-06-27 | 1996-06-26 | Procede et dispositif permettant de produire du gaz combustible |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0850289A1 EP0850289A1 (fr) | 1998-07-01 |
EP0850289B1 true EP0850289B1 (fr) | 2000-01-05 |
Family
ID=6918210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP96942977A Expired - Lifetime EP0850289B1 (fr) | 1995-06-27 | 1996-06-26 | Procede et dispositif permettant de produire du gaz combustible |
Country Status (16)
Country | Link |
---|---|
US (1) | US5961673A (fr) |
EP (1) | EP0850289B1 (fr) |
JP (1) | JPH11509242A (fr) |
KR (1) | KR19990028458A (fr) |
CN (1) | CN1076388C (fr) |
AT (1) | ATE188503T1 (fr) |
AU (1) | AU708656B2 (fr) |
CA (1) | CA2225612C (fr) |
CZ (1) | CZ286257B6 (fr) |
DK (1) | DK0850289T3 (fr) |
EA (1) | EA000184B1 (fr) |
ES (1) | ES2143251T3 (fr) |
GR (1) | GR3033081T3 (fr) |
HU (1) | HU219421B (fr) |
PL (1) | PL181536B1 (fr) |
WO (2) | WO1997001617A1 (fr) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1203802A1 (fr) * | 2000-11-02 | 2002-05-08 | Registrar, Indian Institute of Science | Installation de gazéification de biomasse |
AUPR229100A0 (en) | 2000-12-22 | 2001-01-25 | Renewable Energy Corporation Limited | Grate structure for solid fuel burners |
US6497187B2 (en) * | 2001-03-16 | 2002-12-24 | Gas Technology Institute | Advanced NOX reduction for boilers |
KR100454235B1 (ko) * | 2002-01-29 | 2004-10-26 | 한국과학기술원 | 페이스트형 살충제 및 이의 제조방법 |
ES2206056B1 (es) * | 2002-10-25 | 2005-04-16 | Alberto Ignacio Gonzalo Callejo | Proceso de generacion de calor mediante la combustion de biomasa en dos etapas. |
CZ2006108A3 (cs) * | 2006-02-20 | 2007-08-01 | Ecosource S. R. O. | Zpusob zplynování biochemických a chemických látek s vyuzitím elektrického oblouku a zarízení k provádení tohoto zpusobu |
DE102008043131B4 (de) * | 2008-10-23 | 2012-09-20 | Burkhardt Gmbh | Verfahren und Vorrichtung zum thermochemischen Vergasen fester Brennstoffe |
DE202009002781U1 (de) * | 2009-02-27 | 2009-06-10 | Kbi International Ltd. | Reaktor zur thermischen Behandlung eines Einsatzstoffs |
ES2390146B1 (es) * | 2011-02-15 | 2013-09-19 | José RIBA PICOLA | Sistema para gasificar biomasa combustible y procedimiento de gasificación de biomasa combustible |
RU2662440C1 (ru) * | 2017-09-25 | 2018-07-26 | Федеральное государственное унитарное предприятие "Центр эксплуатации объектов наземной космической инфраструктуры" (ФГУП "ЦЭНКИ") | Способ газификации твердого топлива и устройство для его осуществления |
CN108929720B (zh) * | 2018-07-10 | 2020-09-15 | 太原理工大学 | 一种自气化热解焦油气化炉 |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE377222C (de) * | 1921-03-15 | 1923-06-13 | Josef Martin | Treppenrost mit bewegten Schuerrosten fuer Gaserzeuger |
GB377767A (en) * | 1931-05-12 | 1932-08-04 | Thomas Roland Wollaston | Improvements in and relating to furnaces of gas-producer type for firing steam boilers and like apparatus |
DE926978C (de) * | 1948-10-02 | 1955-04-28 | Josef Muenster | Gaserzeuger |
DE3042200A1 (de) * | 1980-11-08 | 1982-06-16 | Klöckner-Humboldt-Deutz AG, 5000 Köln | Vorrichtung zur gewinnung von grossen mengen an brennbarem gas aus kohlenstoffhaltigen materialien |
US4388082A (en) * | 1981-11-03 | 1983-06-14 | Klockner-Humboldt-Deutz Ag | Device for obtaining large amounts of combustible gas from carbonaceous materials |
DE3312863C2 (de) * | 1983-04-09 | 1986-12-04 | Kernforschungsanlage Jülich GmbH, 5170 Jülich | Brennkammer zum Verbrennen von Abgasen |
DE3409292C2 (de) * | 1984-03-14 | 1986-07-31 | Manfred 4440 Rheine Köpke | Feststoffvergasungsheizkessel |
US4747355A (en) * | 1986-02-14 | 1988-05-31 | Berkum Robert A Van | Combustion apparatus and method of generating gas |
DE3705406A1 (de) * | 1987-02-20 | 1988-09-08 | Manfred Koepke | Feststoffvergasungsheizkessel |
DE3816085A1 (de) * | 1988-05-11 | 1989-11-23 | Deilmann Ag C | Verfahren und vorrichtung von bevorzugt in feuerungsanlagen nutzbarem gas aus problematischem vergasungsgut |
IT1236318B (it) * | 1989-11-29 | 1993-02-09 | Tomadini Gino & C | Apparecchiatura di gassificazione di combustibili solidi |
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1995
- 1995-06-27 WO PCT/DE1995/000816 patent/WO1997001617A1/fr active Application Filing
-
1996
- 1996-06-26 CN CN96195129A patent/CN1076388C/zh not_active Expired - Fee Related
- 1996-06-26 JP JP9504087A patent/JPH11509242A/ja active Pending
- 1996-06-26 EP EP96942977A patent/EP0850289B1/fr not_active Expired - Lifetime
- 1996-06-26 PL PL96324349A patent/PL181536B1/pl not_active IP Right Cessation
- 1996-06-26 KR KR1019970709774A patent/KR19990028458A/ko not_active Application Discontinuation
- 1996-06-26 CZ CZ19974032A patent/CZ286257B6/cs not_active IP Right Cessation
- 1996-06-26 AT AT96942977T patent/ATE188503T1/de not_active IP Right Cessation
- 1996-06-26 US US08/981,016 patent/US5961673A/en not_active Expired - Lifetime
- 1996-06-26 WO PCT/DE1996/001122 patent/WO1997001618A1/fr not_active Application Discontinuation
- 1996-06-26 CA CA002225612A patent/CA2225612C/fr not_active Expired - Fee Related
- 1996-06-26 HU HU9900770A patent/HU219421B/hu not_active IP Right Cessation
- 1996-06-26 DK DK96942977T patent/DK0850289T3/da active
- 1996-06-26 EA EA199800094A patent/EA000184B1/ru not_active IP Right Cessation
- 1996-06-26 AU AU61874/96A patent/AU708656B2/en not_active Ceased
- 1996-06-26 ES ES96942977T patent/ES2143251T3/es not_active Expired - Lifetime
-
2000
- 2000-03-28 GR GR20000400770T patent/GR3033081T3/el not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
PL181536B1 (pl) | 2001-08-31 |
CZ286257B6 (cs) | 2000-02-16 |
CN1076388C (zh) | 2001-12-19 |
JPH11509242A (ja) | 1999-08-17 |
HU219421B (hu) | 2001-04-28 |
KR19990028458A (ko) | 1999-04-15 |
HUP9900770A3 (en) | 1999-11-29 |
WO1997001617A1 (fr) | 1997-01-16 |
ATE188503T1 (de) | 2000-01-15 |
WO1997001618A1 (fr) | 1997-01-16 |
US5961673A (en) | 1999-10-05 |
GR3033081T3 (en) | 2000-08-31 |
DK0850289T3 (da) | 2000-06-13 |
AU6187496A (en) | 1997-01-30 |
ES2143251T3 (es) | 2000-05-01 |
HUP9900770A2 (hu) | 1999-07-28 |
AU708656B2 (en) | 1999-08-12 |
PL324349A1 (en) | 1998-05-25 |
CZ403297A3 (cs) | 1998-07-15 |
EP0850289A1 (fr) | 1998-07-01 |
EA000184B1 (ru) | 1998-12-24 |
CN1189184A (zh) | 1998-07-29 |
EA199800094A1 (ru) | 1998-08-27 |
CA2225612A1 (fr) | 1997-01-16 |
CA2225612C (fr) | 2002-04-23 |
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