EP1447438A1 - Vierzug-Vergasung - Google Patents
Vierzug-Vergasung Download PDFInfo
- Publication number
- EP1447438A1 EP1447438A1 EP03002689A EP03002689A EP1447438A1 EP 1447438 A1 EP1447438 A1 EP 1447438A1 EP 03002689 A EP03002689 A EP 03002689A EP 03002689 A EP03002689 A EP 03002689A EP 1447438 A1 EP1447438 A1 EP 1447438A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- coke
- gasification
- screw
- air
- 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
Links
Images
Classifications
-
- 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
- C10J3/007—Screw type gasifiers
-
- 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
- C10J3/06—Continuous processes
- C10J3/10—Continuous processes using external heating
-
- 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
- C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
- C10J3/60—Processes
- C10J3/62—Processes with separate withdrawal of the distillation products
-
- 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
-
- 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
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
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- 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
-
- 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
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/158—Screws
-
- 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
- C10J2300/0916—Biomass
-
- 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
- C10J2300/0943—Coke
-
- 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
- C10J2300/12—Heating the gasifier
- C10J2300/1223—Heating the gasifier by burners
-
- 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
- C10J2300/1609—Post-reduction, e.g. on a red-white-hot coke or coal 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
- C10J2300/00—Details of gasification processes
- C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
- C10J2300/1846—Partial oxidation, i.e. injection of air or oxygen only
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/304—Burning pyrosolids
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/80—Furnaces with other means for moving the waste through the combustion zone
- F23G2203/801—Furnaces with other means for moving the waste through the combustion zone using conveyors
- F23G2203/8013—Screw conveyors
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2207/00—Control
- F23G2207/10—Arrangement of sensing devices
- F23G2207/101—Arrangement of sensing devices for temperature
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/26—Biowaste
Definitions
- the invention relates to a four-pass carburetor in the Biomass or similar materials with a lack of oxygen be gassed. This gas can be used for the operation of Internal combustion engines or gas burners are used.
- the present invention relates to a four-pass carburetor in which the entire gasification process takes place in four passes.
- Train 1 The material to be gasified is located in the material supply container 3.
- a screw conveyor 5 which is located inside the gasification channel the material from the hopper 3, is transported into the hopper. 6
- the drive for this 4 is infinitely variable, since the transport speed depends on the structure and the moisture of the material to be gasified. Due to the high temperature above the gasification channel, the material is heated at temperatures around 1000 ° Celsius. The material is dried, the rapidly volatile gases escape and pre-pyrolyzing takes place. At the end of the screw conveyor 5 , the material falls into the filling shaft 6.
- Train 2 There is a transport spiral 9 in the depression of the gasification channel . This transport spiral transports the pre-pyrolyzed material from the filling shaft 6 to the ash discharge nozzle 11. At various points 24 , preheated gasification air is supplied so that on the way from the filling shaft 6 to the ash discharge 11 . the entire material is gasified and at the end of the gasification duct, outgassed material is produced in the form of ash.
- Train 3 At the end of the gasification channel, the gas collects and flows into the hot gas pipe 12. In this pipe, the gas reaches the gas shaft 13 in the absence of oxygen and flows via the stand pipe 14 into the coke screw.
- item 12 a short spiral, which is located in the hot gas pipe, is driven via the same chain drive. This short spiral has the task of transporting back the dust particles or suspended matter entrained in the gas and at the same time the gas is to be swirled by the shape of the spiral.
- the hot gas tube 12 has the task of giving the gas a longer dwell time so that the thermal conversion process can be carried out with the addition of externally supplied heat.
- Train 4 The gas flows from the hot gas pipe 12 , into the gas shaft 13 and then through the standpipe 14, into the coke screw.
- this coke screw which is double-walled and is cooled from the outside by the gasification air, the gas flows from the inlet connection 14 to the coke tank 16.
- the gas Within this coke screw, the gas is cooled and cleaned by the coke in a countercurrent process. The gas then collects in the coke container 16 and is sucked off by the suction draft 17 and blown to the point of use.
- the gasification duct is heated to approximately 200 ° Celsius by means of a pilot burner 7 .
- industrial coke is fed through the coke screw 15 into the filling shaft 6 .
- the check valve 21 is opened by the coke screw 15 , driven by the motor 20 .
- the coke entered in connection with the heat of the pilot burner quickly generates a process temperature of over 500 ° Celsius.
- gasification material is continuously added to the filling shaft 6 by the material screw 5 , driven by the motor 4 .
- the entire system is operated with an excess of oxygen until the gasification temperature of approx. 1000 ° Celsius is reached. This control takes place via the side channel compressor 22.
- the side channel compressor 22 sucks in the room air or oxygen-enriched air and presses it into the piping system 23 .
- the air enters the gap in the double-walled coke screw 15 and flows through this gap, which is provided with hospital-shaped air baffles, up to the starting point 23. This ensures that the coke, which is intended to cool the gas, is cooled from the outside to reach a hot gasification air at the same time. After the hot gasification air has escaped from the annular gap of the coke screw, the hot air is conducted in an insulated pipe 23 to the individual injection points.
- the object of the invention is a fully automatic operation of the four-pass carburetor.
- a level indicator 1 is installed in the material storage container.
- a transport screw is switched which conveys material into the container 3 via the opened pinch valve 2 .
- the amount of material is determined by the continuously variable drive motor 4 .
- the drive motor 20 for the coke screw runs only at intervals in order to transport hot coke loaded in cycles through the non-return flap 21 into the filling shaft 6 .
- the intervals for the cycle times of the coke screw depend on the outflow temperature of the gas from the coke container 16. Also in this container, a level indicator is installed which controls the transport screw for the coke when necessary and at the same time the pinch valve 19 is opened.
- the entire four-pass carburetor has high temperatures of up to 1000 ° Celsius, the entire gasification duct is covered with high-quality insulation 29 .
- the entire carburettor unit can be mounted on a base frame and, thanks to its narrow, long and low shape, forms an inexpensive installation option in rooms.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
Claims (9)
- Vorrichtung zur Erzeugung eines Gases aus Biomasse oder ähnlichen Material. Dadurch gekennzeichnet, dass das Material durch eine innenliegende Schnecke vorpyrolisiert wird.
- Verfahren nach Anspruch 1) dadurch gekennzeichnet, dass das vorpyrolysierte Material in einem mindestens 6,00 m langen Vergasungskanal mittels einer Spirale vom Einfüllschacht bis zur Ascheaustragung mechanisch transportiert wird.
- Verfahren nach Anspruch 2) dadurch gekennzeichnet, dass die erzeugten Gase in einem ebenfalls innenliegenden Heissgasrohr, durch die von aussen extern zugeführte Hitze nachvergast werden und dadurch eine längere Verweilzeit erhalten.
- Verfahren nach Anspruch 3) dadurch gekennzeichnet, dass die Gase durch einen Gaskanal, der doppelwandigen Koksschnecke zugeführt und im Gegenstromverfahren durch den Koks abgekühlt und gereinigt werden.
- Verfahren nach Anspruch 4) dadurch gekennzeichnet, dass der erhitzte und belastete Industriekoks, in Intervallen dem Vergaser wieder zugeführt wird.
- Verfahren nach Anspruch 5) dadurch gekennzeichnet, dass die verbrauchte Koksmenge, automatisch in den Vorratsbehälter wieder nachgefüllt wird.
- Verfahren nach Anspruch 6) dadurch gekennzeichnet, dass die Temperatursteuerung in dem Vergaser durch Thermoelemente und stufenlos regelbare Kugelventile von einer SPS - Steuerung automatisch geregelt wird.
- Verfahren nach Anspruch 7) dadurch gekennzeichnet, dass am Ende des Heissgasrohres eine angetriebene Spirale vorhanden ist, die eventuelle Ablagerungen die im Heissgas auftreten können, wieder zum Ausgang zurücktransportiert. Gleichzeitig werden die Gase in eine Wirbelströmungversetzt.
- Verfahren nach Anspruch 8) dadurch gekennzeichnet, dass sich in dem Ringspalt der doppelwandigen Koksschnecke Luftleitbleche befinden, die erreichen, dass sich die Vergasungsluft umlaufend um die innenliegende Koksschnecke bewegt und daher einen längeren Weg für die Kühlung und gleichzeitige Aufheizung der Vergasungsluft erreicht wird.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP03002689.2A EP1447438B1 (de) | 2003-02-12 | 2003-02-12 | Vergasung mit Vorpyrolysierung von Biomasse und zusätzlicher Vergasung der Gase |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP03002689.2A EP1447438B1 (de) | 2003-02-12 | 2003-02-12 | Vergasung mit Vorpyrolysierung von Biomasse und zusätzlicher Vergasung der Gase |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1447438A1 true EP1447438A1 (de) | 2004-08-18 |
EP1447438B1 EP1447438B1 (de) | 2015-07-08 |
Family
ID=32668950
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03002689.2A Expired - Lifetime EP1447438B1 (de) | 2003-02-12 | 2003-02-12 | Vergasung mit Vorpyrolysierung von Biomasse und zusätzlicher Vergasung der Gase |
Country Status (1)
Country | Link |
---|---|
EP (1) | EP1447438B1 (de) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006019452A1 (de) * | 2006-04-24 | 2007-10-25 | Rew Regenerative Energie Wirtschaftssysteme Gmbh | Biomassevergaser |
EP1865045A1 (de) * | 2006-06-07 | 2007-12-12 | ILW - Ingeneurbüro | Dampfreformator für Biomasse |
WO2011101020A1 (de) * | 2010-02-16 | 2011-08-25 | Gim Holding Bv | Verfahren und vorrichtung zur gewinnung von brennbaren treibstoffen und gasen aus organischen stoffen |
EP2769148A4 (de) * | 2011-10-21 | 2015-11-04 | Therma Flite Inc | Vergasungsvorrichtung und verfahren sowie abfallbehandlungssystem und verfahren damit |
CN115247084A (zh) * | 2022-07-07 | 2022-10-28 | 重庆科技学院 | 基于生物质自热源热解气化的高品质合成气制备系统 |
DE102022001817A1 (de) | 2022-05-24 | 2023-11-30 | Biomass-to-hydrogen GmbH | Verfahren zur Synthesegasgewinnung aus kohlenstoffhaltigen Reststoffen in einem Reaktor mit Helix-förmiger Durchströmung |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996032163A1 (en) | 1995-04-11 | 1996-10-17 | Moraski Dennis P | Biomass solids gasification system and process |
US6024032A (en) * | 1995-10-26 | 2000-02-15 | Compact Power Limited | Production of heat energy from solid carbonaceous fuels |
WO2001068789A1 (en) * | 2000-03-15 | 2001-09-20 | Cowi Rådgivende Ingeniører As | A method and a system for decomposition of moist fuel or other carbonaceous materials |
EP1323810A1 (de) | 2001-12-12 | 2003-07-02 | von Görtz & Finger Techn. Entwicklungs Ges.m.b.H. | Doppelrohrvergaser |
-
2003
- 2003-02-12 EP EP03002689.2A patent/EP1447438B1/de not_active Expired - Lifetime
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996032163A1 (en) | 1995-04-11 | 1996-10-17 | Moraski Dennis P | Biomass solids gasification system and process |
US6024032A (en) * | 1995-10-26 | 2000-02-15 | Compact Power Limited | Production of heat energy from solid carbonaceous fuels |
WO2001068789A1 (en) * | 2000-03-15 | 2001-09-20 | Cowi Rådgivende Ingeniører As | A method and a system for decomposition of moist fuel or other carbonaceous materials |
EP1323810A1 (de) | 2001-12-12 | 2003-07-02 | von Görtz & Finger Techn. Entwicklungs Ges.m.b.H. | Doppelrohrvergaser |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102006019452A1 (de) * | 2006-04-24 | 2007-10-25 | Rew Regenerative Energie Wirtschaftssysteme Gmbh | Biomassevergaser |
WO2007121733A2 (de) * | 2006-04-24 | 2007-11-01 | Rew Regenerative Energie Wirtschaftssysteme Gmbh | Biomassevergaser und verfahren zur allothermen vergasung von biomasse |
WO2007121733A3 (de) * | 2006-04-24 | 2007-12-06 | Dieter Schillingmann | Biomassevergaser und verfahren zur allothermen vergasung von biomasse |
DE102006019452B4 (de) * | 2006-04-24 | 2008-05-08 | Rew Regenerative Energie Wirtschaftssysteme Gmbh | Biomassevergaser |
EP1865045A1 (de) * | 2006-06-07 | 2007-12-12 | ILW - Ingeneurbüro | Dampfreformator für Biomasse |
WO2011101020A1 (de) * | 2010-02-16 | 2011-08-25 | Gim Holding Bv | Verfahren und vorrichtung zur gewinnung von brennbaren treibstoffen und gasen aus organischen stoffen |
EP2769148A4 (de) * | 2011-10-21 | 2015-11-04 | Therma Flite Inc | Vergasungsvorrichtung und verfahren sowie abfallbehandlungssystem und verfahren damit |
US9446975B2 (en) | 2011-10-21 | 2016-09-20 | Therma-Flite, Inc. | Gasifying system and method |
DE102022001817A1 (de) | 2022-05-24 | 2023-11-30 | Biomass-to-hydrogen GmbH | Verfahren zur Synthesegasgewinnung aus kohlenstoffhaltigen Reststoffen in einem Reaktor mit Helix-förmiger Durchströmung |
CN115247084A (zh) * | 2022-07-07 | 2022-10-28 | 重庆科技学院 | 基于生物质自热源热解气化的高品质合成气制备系统 |
CN115247084B (zh) * | 2022-07-07 | 2023-11-03 | 重庆科技学院 | 基于生物质自热源热解气化的高品质合成气制备系统 |
Also Published As
Publication number | Publication date |
---|---|
EP1447438B1 (de) | 2015-07-08 |
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