EP0055840A1 - Procédé et installation pour la combustion de matières organiques - Google Patents

Procédé et installation pour la combustion de matières organiques Download PDF

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Publication number
EP0055840A1
EP0055840A1 EP81110617A EP81110617A EP0055840A1 EP 0055840 A1 EP0055840 A1 EP 0055840A1 EP 81110617 A EP81110617 A EP 81110617A EP 81110617 A EP81110617 A EP 81110617A EP 0055840 A1 EP0055840 A1 EP 0055840A1
Authority
EP
European Patent Office
Prior art keywords
gasification
shaft
chamber
degassing
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.)
Granted
Application number
EP81110617A
Other languages
German (de)
English (en)
Other versions
EP0055840B1 (fr
Inventor
Heinz Mallek
Manfred Dr. Laser
Dorothee Ermisch
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.)
Forschungszentrum Juelich GmbH
Original Assignee
Forschungszentrum Juelich GmbH
Kernforschungsanlage Juelich GmbH
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
Application filed by Forschungszentrum Juelich GmbH, Kernforschungsanlage Juelich GmbH filed Critical Forschungszentrum Juelich GmbH
Priority to AT81110617T priority Critical patent/ATE12681T1/de
Publication of EP0055840A1 publication Critical patent/EP0055840A1/fr
Application granted granted Critical
Publication of EP0055840B1 publication Critical patent/EP0055840B1/fr
Expired legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • 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
    • 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
    • C10J3/30—Fuel charging devices
    • 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
    • C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
    • C10J3/60—Processes
    • C10J3/64—Processes with decomposition of the distillation products
    • C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
    • 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
    • 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
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • 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
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0956—Air or oxygen enriched air
    • 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
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0959—Oxygen
    • 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
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0969—Carbon dioxide
    • 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
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0973—Water
    • C10J2300/0976—Water as steam
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00—Pretreatment
    • F23G2201/40—Gasification

Definitions

  • the invention relates to a method for incinerating waste from organic substances, in which the waste from organic substances is first dried and degassed in the absence of air at temperatures rising up to about 550 ° C. and then in a continuous flow of material at temperatures up to about 850 ° C are mainly gasified, whereupon the gases formed in whole or in part and the remaining combustible solid products together with the ashes formed during the gasification are brought into a combustion chamber with fresh air supply, and a device for carrying out this method.
  • Methods and devices for burning waste from organic substances belong to the known prior art.
  • a method of the aforementioned type is known, in which the waste materials first dried, then degassed and then gasified and the pretreated gaseous and solid products are then burned. The drying, degassing, gasification and combustion processes run continuously.
  • an ember bed is formed from the exhaust gas products entering the gasification chamber.
  • air is passed into the gasification zone in sufficient quantity so that the ember bed has a volume and temperature level which is sufficient for the intended purpose.
  • the invention has for its object to provide a method and a device suitable for carrying out the method, with which it is possible to handle larger throughputs of waste materials than is possible with the known devices.
  • This object is achieved according to the invention in a method of the type mentioned above in that the drying, degassing and gasification of the waste materials is carried out in two procedurally separate steps, in that the waste materials are dried and degassed in a first step, and this during degassing resulting material is gasified in a second step, the substances being guided in such a way that the material flow between the first and the second process step can be interrupted for the purpose of mechanical treatment of the material resulting from the degassing and that the degassed material is gasified at the beginning of the process Gasification phase the amounts of gasifying agents such as air, steam, C0 2 , 0 2 or a mixture of these substances is added to the changes in the composition of the material during the flow of material.
  • the drying, degassing and gasification of the waste materials is carried out in two procedurally separate steps, in that the waste materials are dried and degassed in a first step, and this during degassing resulting material is gasified in a second step, the substances being guided in such a way
  • the gasification means are supplied to the substances to be gasified from the start during the gasification process in cocurrent. Through this as well as through the Separation of the drying and degassing step from the gasification step ensures that the gasification process is far more manageable than before, because the addition of gasifying agents can be controlled in a simple manner depending on the composition of the gases formed during the gasification and the solid combustible substances.
  • the gasification agent is supplied to the material to be gasified in the direction of flow of the material together with gases formed during drying and degassing.
  • the steam released during drying with the formation of water gas for the gasification of carbon, and the smoldering gases produced during the degassing of the wastes, for cracking the long-chain hydrocarbon molecules into low-molecular compounds, are conducted at the gasification temperature over the coke formed during the degassing.
  • the fuel gas developed during the gasification is removed via a gap-shaped passage, the material being held above the gap until it is gasified.
  • a preferred device for carrying out the method according to the invention is a device with a shaft furnace for carrying out the method according to claims 1 to 4 with a device for emitting heat for gasifying the material in the shaft, with a combustion chamber downstream of the shaft, wherein in the Combustion chamber opening burners as well as combustion air inlets and an extraction device for the ashes are provided at the bottom of the combustion chamber.
  • the device bearing shaft furnace is designed according to the invention in that one is provided for pretreating the waste organic materials by the action of heat with exclusion of air at temperatures up to serving to about 55 0 0 C chamber first to the shaft as a second, the effect of heat of the substances at higher temperatures serving chamber is connected, with at the upper part of the shaft in the gasification chamber leads to a feed for the gasification agent to be added to the gas to be gasified and the shaft from the combustion chamber through a constricting passage with the supply of the material to be burned regulating structure elements is separated.
  • the advantage here is that the passage is designed as an annular or longitudinal gap.
  • a shaft furnace for the disposal of waste With a combustion chamber provided in the shaft furnace, e.g. known from DE-OS 26 o4 4o9.
  • a combustion chamber provided in the shaft furnace
  • fresh air supplies to the combustion chamber and flue gas discharges from the combustion chamber are provided.
  • a constriction is provided at the transition from the shaft of the shaft furnace to the combustion chamber, in the immediate vicinity of which the fresh air feeds open.
  • the waste to be removed is dried, degassed, gasified and then the remaining coke residues are burned together with the fuel gas produced.
  • the shaft furnace in which gasification and combustion are carried out is preceded by a heated chamber in which the organic substances are dried and degassed.
  • exhaust gas channels are connected to the shaft, which in their course surround the outer wall of the first chamber.
  • a particularly advantageous embodiment of the device with shaft furnace according to the invention is that for the pretreatment of the waste the first chamber determined by drying and degassing is designed as a rotating drum inclined to the horizontal with a gas-tight lock system at the loading end, the other end of which opens at the upper part of the chamber forming the gasification chamber, so that the material subjected to the heat treatment after being discharged from the rotating drum got into the furnace shaft.
  • the device according to the invention with drying and Ent is a continuous process Gasification of organic waste separated from gasification and subsequent combustion. This is done in that the drying and degassing are carried out with exclusion of air in the externally heated rotary drum and the gasification with the addition of gasifying agents in the shaft furnace. By separating the drying and degassing process from the gasification and subsequent combustion process it is achieved that the processes are easier to control and in the gasification stage a fuel gas of uniform quality is generated which leads to a complete combustion of the waste material.
  • the device according to the invention in such a way that between the end of the rotary drum and the shaft which is subject to drying and degassing, the end of the shaft furnace spanning the upper part of the shaft , is provided by means of one or more gas-tight locks lockable intermediate chamber.
  • the device according to To design the invention so that the upper part of the shaft is completely or partially covered by a vibrating screen and that on the side opposite the confluence of the rotating drum in the upper part of the shaft furnace with a lower surface at the level of the vibrating screen, lockable shaft by means of a gas-tight lock is provided for discharging non-combustible goods.
  • a closure flap is provided above the ash outlet, which is arranged at a sufficient distance from the narrow point provided in the shaft of the shaft furnace.
  • the waste is fed into the rotary drum 2 via a filling sluice 1 arranged at one end of the rotary drum 2 which is inclined with respect to the horizontal.
  • the waste is dried and degassed in the rotary drum 2, which is heated to approximately 550 ° C.
  • the rotary drum 2 can be heated. This can be done either directly by arranging burners or expediently in that the flue gas line 11 connected to the combustion chamber 6 in the lower part of the shaft furnace 4 is guided in such a way that it surrounds the rotary drum 2 in its course with the line section 3 so that the The outer wall of the rotary drum 2 also forms an inner wall of the section 3 of the flue gas line 11.
  • the rotary drum 2 to the upper part of the shaft furnace 4 is connected so that the rotary drum 2 in theIndiaglall - is further funneled te Good after drying and devolatilization in the shaft of the shaft furnace.
  • the shaft of the shaft furnace 4 forms the gasification space 6a.
  • the gasification chamber 6a opens a feed line 5 for the Ver to be added gas agent.
  • the gasification chamber 6a is separated from the downstream combustion chamber 6 by one or more lock elements 7.
  • the lock elements 7 have a closed upper side with respect to the gasification chamber and are mounted on a shaft or axis which, during their movement, release gap-shaped through openings for the discharge of the solid and gaseous products from the gasification chamber 6a into the combustion chamber 6.
  • Combustion air feeds 8 open into the combustion chamber below the lock elements 7, and one or more burners 9 are also arranged on the combustion chamber 6, only one of which is shown in the drawing.
  • Smoke gases generated during combustion are discharged through an exhaust pipe 11 connected to the combustion chamber.
  • the solid components entering the combustion chamber 6 are deposited on the closure flap 1o, which forms the bottom of the combustion chamber. It is arranged at a distance from the lock elements 7 such that the combustion chamber has a sufficient volume.
  • the arrangement of a closure flap 10 in the combustion chamber 6 has the advantage that the complete further transfer of the ash formed during the combustion is facilitated in accordance with the respective amount of ash removal 12.
  • the end of the rotating drum 2, from which the filled goods are passed on after drying and degassing does not open directly into the shaft of the shaft furnace 4, but into one arranged between the rotating drum and shaft furnace , by means of locks 13 and 14 gas-tight lockable intermediate chamber 15, which overlaps the upper part of the shaft of the shaft furnace 4--.
  • the shaft is covered by a vibrating screen 16. This has the advantage that through the vibrating screen 16 in the shaft of the shaft furnace 4 and thus in the combustion chamber 6a, in the upper part of which the feed line 5 for the gasification agents to be added also opens, only gaseous products and such solid products pass through the mesh of the vibrating screen can fall through.
  • a tubular part 18 rotatable about its longitudinal axis in the shaft of the shaft furnace 4 with a part 19 which widens conically at the end protruding into the shaft, between the gasification chamber 6a and the combustion chamber 6 between the base of the conical one Part 19 and the adjacent wall of the furnace shaft formed a constriction formed as an annular gap.
  • the tubular part 18 is rotatable about its longitudinal axis, especially when the tubular part 18 protruding laterally into the shaft - not shown in the drawing - are arranged during the gasification, a loosening of the material to be gasified .
  • the tubular part 18 also serves to supply air to the combustion chamber.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)
EP81110617A 1980-12-27 1981-12-19 Procédé et installation pour la combustion de matières organiques Expired EP0055840B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81110617T ATE12681T1 (de) 1980-12-27 1981-12-19 Verfahren und einrichtung zum verbrennen von organischen stoffen.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3049250 1980-12-27
DE3049250A DE3049250C2 (de) 1980-12-27 1980-12-27 Einrichtung mit Schweldrehtrommel und Schachtofen

Publications (2)

Publication Number Publication Date
EP0055840A1 true EP0055840A1 (fr) 1982-07-14
EP0055840B1 EP0055840B1 (fr) 1985-04-10

Family

ID=6120429

Family Applications (1)

Application Number Title Priority Date Filing Date
EP81110617A Expired EP0055840B1 (fr) 1980-12-27 1981-12-19 Procédé et installation pour la combustion de matières organiques

Country Status (6)

Country Link
US (1) US4544374A (fr)
EP (1) EP0055840B1 (fr)
JP (1) JPS57133189A (fr)
KR (1) KR880002401B1 (fr)
AT (1) ATE12681T1 (fr)
DE (1) DE3049250C2 (fr)

Cited By (5)

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Publication number Priority date Publication date Assignee Title
GB2136939A (en) * 1983-03-23 1984-09-26 Skf Steel Eng Ab Method for destroying refuse
FR2664169A1 (fr) * 1990-07-05 1992-01-10 Hartmann Helmut Procede pour le traitement de residus organiques toxiques.
EP0555501A1 (fr) * 1992-02-12 1993-08-18 Kiyoharu Michimae Incinérateur du type à distillation sèche
EP0563777A3 (en) * 1992-03-24 1993-11-18 Thyssen Still Otto Gmbh Process and apparatus for production of synthesis gas by thermal treatment of raw materials containing metallic and organic substances
US6251148B1 (en) 1991-07-15 2001-06-26 John Brown Deutsche Entineering Gmbh Process for producing synthetic gasses

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AU8961682A (en) * 1982-08-18 1984-02-23 Rogers, C.D. Biomass gasification
AT382712B (de) * 1985-05-10 1987-04-10 Voest Alpine Ag Beschickungsvorrichtung fuer einen schachtofen zum brennen von karbonathaltigem, mineralischem brenngut
US4738206A (en) * 1986-09-16 1988-04-19 Roy F. Weston, Inc. Apparatus and method for low temperature thermal stripping of volatile organic compounds from soil
USRE33776E (en) * 1986-09-16 1991-12-24 Roy F. Weston, Inc. Apparatus and method for low temperature thermal stripping of volatile organic compounds from soil
US4951417A (en) * 1987-04-03 1990-08-28 Canonie Environmental Services Corp. Method of contaminated soil remediation and apparatus therefor
DE3730729A1 (de) * 1987-09-12 1989-03-30 Gutehoffnungshuette Man Anlage zum verschwelen von abfallstoffen und verunreinigten stoffen
US4864942A (en) * 1988-01-14 1989-09-12 Chemical Waste Management Inc. Process and apparatus for separating organic contaminants from contaminated inert materials
DE3828534A1 (de) * 1988-08-23 1990-03-08 Gottfried Dipl Ing Roessle Verfahren zur verwertung von energiehaltiger masse, vorrichtung zur durchfuehrung des verfahrens und verwendung eines bei der verwertung anfallenden produkts
US5176087A (en) * 1991-12-17 1993-01-05 Roy F. Weston, Inc. Apparatus and method for low temperature thermal stripping of volatile organic compounds from soil and waste materials with non-oxidative cross-sweep gases
US5188041A (en) * 1991-12-17 1993-02-23 Roy F. Weston, Inc. Apparatus and method for low temperature thermal stripping of volatile organic compounds from soil and waste materials with non-oxidative co-current gases
US5588381A (en) * 1995-03-07 1996-12-31 Leslie Technologies, Inc. Method and system for burning waste materials
JPH09208968A (ja) * 1996-01-29 1997-08-12 Mitsubishi Heavy Ind Ltd 廃棄物のガス化処理方法
US6001144A (en) * 1996-01-29 1999-12-14 Mitsubishi Jukogyo Kabushiki Kaisha Waste treatment process
JP3266591B2 (ja) * 1999-12-10 2002-03-18 アートセラミック株式会社 断続流動式熱分解装置
AU2028802A (en) * 2000-12-08 2002-06-18 Janusz Franciszek Luterek Process and gas generator for generating fuel gas
DE10224018B4 (de) * 2002-05-28 2015-10-08 Bioenergy Systems N.V. Vorrichtung und Verfahren zur Energiegewinnung aus Bioenergieträgern und anderen organischen Stoffen
DE102004002043A1 (de) * 2004-01-15 2005-08-04 Maerz Ofenbau Ag Verfahren zum Brennen von körnigem, mineralischem Brenngut
ITRM20050207A1 (it) * 2005-05-02 2006-11-03 Pyrolb S R L Procedimento integrato per il trattamento di rifiuti mediante pirolisi e relativo impianto.
WO2011024145A2 (fr) * 2009-08-27 2011-03-03 Inbicon A/S Procédés et dispositifs pour le pompage de particules
CN108975268B (zh) * 2018-09-10 2022-05-24 浙江工业职业技术学院 一种新能源汽车用氢气制造设备
CO2020004451A1 (es) * 2020-04-14 2020-05-15 Biotecnologia Y Bioingenieria Core S A Reactor vertical continuo multifásico para la producción limpia de hidrocarburos y energía y proceso termoquímico realizado

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DE655843C (de) * 1934-10-28 1938-01-24 Humboldt Deutzmotoren Akt Ges Gaserzeuger fuer bituminoese Brennstoffe mit schwer schmelzender Schlacke, wie z. B.Holz, mit absteigender Vergasung
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KR880002401B1 (ko) 1988-11-04
DE3049250A1 (de) 1982-09-09
US4544374A (en) 1985-10-01
DE3049250C2 (de) 1985-10-24
JPH0451597B2 (fr) 1992-08-19
ATE12681T1 (de) 1985-04-15
EP0055840B1 (fr) 1985-04-10
JPS57133189A (en) 1982-08-17
KR830008108A (ko) 1983-11-09

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