WO2009033543A1 - Verfahren und vorrichtung zur behandlung von beladenem heissgas - Google Patents
Verfahren und vorrichtung zur behandlung von beladenem heissgas Download PDFInfo
- Publication number
- WO2009033543A1 WO2009033543A1 PCT/EP2008/006651 EP2008006651W WO2009033543A1 WO 2009033543 A1 WO2009033543 A1 WO 2009033543A1 EP 2008006651 W EP2008006651 W EP 2008006651W WO 2009033543 A1 WO2009033543 A1 WO 2009033543A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas
- quench
- nozzles
- liquid
- cooling
- Prior art date
Links
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
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
-
- 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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/466—Entrained flow 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
- 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
- C10J3/845—Quench rings
-
- 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
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
- C10K1/06—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials combined with spraying with water
-
- 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
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
-
- 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
- C10J2300/093—Coal
Definitions
- the invention relates to a method and apparatus for the treatment of laden hot gas, preferably in connection with the production of CO and H 2 -containing gases by partial oxidation of substantially dusty and / or liquid feedstocks, in particular ash-containing feedstocks in the air stream, wherein the laden hot gas, in particular containing slag and solid, is transferred from a reaction space into a connected cooling / quench tank, solid and gas are separated and gas is removed from the cooling / quench tank.
- the invention also relates to the use of the device according to the invention.
- a method is known from DD 280975, in which, using spray quenching, cooling water is sprayed over successive nozzle rings with radial components into a gas jet and coaxial components to the gas jet in order to achieve saturation of the water vapor and washing out of solids.
- the with these devices / methods reached operating times of a few weeks and the required high cleaning costs do not meet the requirements for economic operation.
- the object of the invention was therefore to provide a method and a device for treating laden hot gas, with which a transfer of loaded hot gas from a reaction space into a connected refrigerator takes place such that the separation of solid and gas and the gas discharge from the cooling / Quench container with a long service life and low cleaning effort with uncomplicated easy-to-manufacture design is possible.
- laden hot gas is to be understood as meaning a hot gas which contains constituents which, upon cooling, change into the fluid to solid state.
- charged hot gases are in the production of CO and H 2 -containing gases by partial oxidation of substantially dusty and / or liquid feedstocks, in particular special ash-containing feedstocks in the flow stream, gases obtained, containing slag and solid.
- the device according to the invention has a cooling or quenching vessel with gas inlet and gas outlet, in which essentially a first quench space (flash quench space or precursor space) and a second quench space (main quench space) are formed, and which preferably directly from the slag gas outlet Lower part of a gasification reactor can be arranged.
- a first quench space flash quench space or precursor space
- a second quench space main quench space
- Lower part of a gasification reactor can be arranged.
- the separate preferably substantially cylindrical Flashquenchraum is formed in which a pre-quenching takes place and the diameter of about 1.05 to 5 times the inner diameter and its length (in Flow direction of the hot gas) corresponds to about 0.5 to 5 times the inner diameter of the inlet for the loaded hot gas.
- the inlet for the loaded hot gas is preferably the gas slag outlet of the reaction space of a gasification reactor, wherein the gas expediently flows vertically down into the device.
- the Flashquenchraum is advantageously provided with a film-forming device, whereby the inner wall with a film, in particular quench liquid, preferably protected with a water film against heat and encrustations.
- the water film is preferably produced at the upper edge of the flash quench chamber by means of the water film production device and leaves the quench chamber at the lower edge thereof, thus transporting the dripping water into the gas space of the main quench chamber, which is advantageously filled with water in the lower part.
- one or more nozzle rings are arranged, which are designed such that up to about 30 nozzles, preferably 1 to 30 nozzles per 10,000 m 3 i. N. tr. (Dry in the standard state) raw gas (hot gas) are available.
- each nozzle ring has at least 4 individual nozzles.
- the jet direction of the nozzles is on the axis of the loaded hot gas stream (raw gas slag stream) at an angle to the horizontal down, preferably -5 to 30 degrees.
- the hot charged with slag particles raw gas stream with a Quenchcroftkeitsmenge in particular water amount of up to about 50 m 3 , preferably 5 to 50 m 3 per 10,000 m 3 iN tr.
- the outer boundary of the Flashquenchraumes can be designed both cylindrical and frustoconical with larger diameter at the bottom.
- the device according to the invention is equipped in the lower region of the cooling or quenching container with at least one raw gas outlet (outlet for quenched hot gas).
- the device according to the invention is equipped with at least one nozzle ring located behind and / or below the flash quench chamber in order to additionally treat the secondary vortex in the upper part of the main quench chamber.
- the additional nozzle ring is designed so that with a Quench thoroughlykeitsmenge, preferably water amount of up to about 10 m 3 , preferably 1 to 10 m 3 per 1000 m 3 i. N. tr. Crude gas and a nozzle exit velocity of up to about 30m / s, preferably 1 to 10 m / s can be treated.
- Each additional nozzle ring preferably has min. at least 4 individual nozzles.
- the nozzles are designed so that the droplet spectrum of the quench liquid emerging from the nozzles in the range of up to about 500 .mu.m, preferably 50-500 microns.
- the additional nozzle ring expediently the inner surface of the cooling and Quench elementsers is fully applied with a (water) film.
- the device according to the invention has a raw gas outlet arranged essentially in the axis of the main quench chamber, which is preferably equipped with a cone-shaped gas outlet device with a conical tip pointing upwards for the separation of the solids and liquid particles.
- a raw gas outlet arranged essentially in the axis of the main quench chamber, which is preferably equipped with a cone-shaped gas outlet device with a conical tip pointing upwards for the separation of the solids and liquid particles.
- the upper part of the conical gas outlet device is preferably equipped with a spraying device in such a way that a closed (water) film forms on its surface and larger solid particles not yet finally cooled, in particular slag particles, are converted into the solid state and the quench liquid, advantageously water with the slag particles leaves the conical gas outlet device at its lower edge and thus enters the Quench crampkeitssammelraum in the lower part (lower portion) of the Hauptquench mattersers.
- the device according to the invention comprises alternatively to the above-mentioned conical gas outlet device with central learn Rohgasabgang, at least one, substantially horizontally to the outer shell and above the surface of the liquid Quench crampkeitssammel- the space of the main Quench organizations arranged raw gas discharge, preferably 2 to 5 Einzelrohgasab Entryen.
- the at least one raw gas discharge or each of the Einzelrohgasab réelle is expediently equipped in the main quench with arranged above the respective gas outlet flow baffles, which ensure that the flow rate of each flowing into the Einzelrohgasabgang raw gas is the same when leaving the Hauptquenchrau-.
- the Strömungsleitbleche are advantageous conical segments which are attached to the outer shell of the main Quenchraumes with the upper end and inclined down so that the flow lines of the gas flow from the lower deflecting edge of the respective baffle to the middle of the individual gas outlet always have the same length, so that This ensures a rotationally symmetrical gas flow in the main quench space.
- the laterally arranged raw gas outlets are provided with devices which ensure an admission in the flow direction with quench liquid, preferably water, so that the laxative pipe is provided over the entire circumference with a (water) film.
- quench liquid preferably water
- a venturi scrubber for scrubbing crude gas is advantageously arranged in all gas outlets after leaving the cooling and quenching container.
- the device according to the invention is preferably used in such a way that a separate cylindrical flash quench space is arranged directly at the slag gas outlet from a gasification reactor in the upper part of a cooling and quenching container arranged underneath, in which a pre-quenching takes place and with further Nozzle systems of the resulting with the secondary vortex still charged with particulate matter upward gas flow in Quench- and cooling tank, the inner wall of the cooling and quench, the Rohgasaustrittsstrom from the cooling and Quench inherenter and internals in the cooling and Quench variouser, which serve for Rohgasabzug exposed to water become.
- the device according to the invention is preferably used for the treatment of hot pressure gasification gases from entrainment gasifiers.
- the invention also relates to a process for the treatment of laden hot gas, which is preferably the crude gas slag stream originating from a (gas) gasification reactor, wherein quench liquid is injected into the laden hot gas in a first step in an amount of up to about 50 m 3 , preferably from 5 to 50 m 3 per 10,000 m 3 iN tr.
- quench liquid is injected into the laden hot gas in a first step in an amount of up to about 50 m 3 , preferably from 5 to 50 m 3 per 10,000 m 3 iN tr.
- nozzles up to about 30 nozzles, in particular from 1 to 30 nozzles per 10,000 m 3 of iN tr.
- Raw gas unloaded hot gas
- Figure 1 the device of the invention in conjunction with a central raw gas
- Figure 2 the device according to the invention in conjunction with a plurality of laterally disposed raw gas outlets
- the embodiment relates to the use of the invention in a pulverized coal gasifier with integrated quench system.
- the performance of the carburetor is 80,000 m 3 i. N./h dry.
- the cooling and quenching container 13 arranged immediately below the gasification reactor is divided into a flash quenching chamber 1 and a main quenching chamber 2.
- the gas inlet 14 (here: slag exhaust body of the carburettor) has a diameter of 600 mm and a height of 1000 mm.
- the inner side of the cylindrical Flashquenchraumes 1 with a diameter of 800 mm is applied at the top via the water supply 3 with 40 m 3 / h of water via a water annulus, so that a closed downflowing outflowing water film 4 is formed on the inside of the Flashquenchraumes.
- the actual quenching of the gas stream is carried out by means of 30 m 3 / h each of 3 nozzle rings 5, which are each equipped with 8 individual nozzles.
- the jacket of the Flashquenchraumes has at the respective position of the individual nozzles corresponding openings to ensure the entry of the liquid jets 6 with a drop size of 0.5 to 3 mm and a flow rate of 15 m / s in the raw gas stream.
- the secondary vortex 11 generated with the arrangement of the gas outlet device 8 is connected to the 32 spray nozzles arranged in the dome of the main quench tank.
- sen 12 with 60 m 3 / h of water so sprayed that with the setting of the spray direction and the droplet size of 100 to 300 microns intensive contacting of the water droplets with the not yet deposited fine particles in the raw gas and complete wetting of the inner wall of the cooling and quench 2 takes place.
- the alternative solution according to the invention according to FIG. 2 is equipped in the lower tank area with a plurality of gas outlets 15, which are located above the water level 16 and are equipped to separate the solids-water particles with conical flow baffles 17 above the single raw waste gas outlet.
- the lower end 18 of the Einzelleitbleches is geometrically designed so that the flow lines of the gas flow from each point of the lower edge 18 of the guide plate have the same length to the center of the respective Rohgasabzuges 19, whereby a rotationally symmetrical gas flow in the main quench 2 is ensured.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Industrial Gases (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Treating Waste Gases (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0816385-5A2A BRPI0816385A2 (pt) | 2007-09-07 | 2008-08-13 | Processo e dispositivo para o tratamento de gás quente carregado |
CA2698909A CA2698909C (en) | 2007-09-07 | 2008-08-13 | Process and device for treating charged hot gas |
CN2008801057599A CN101809125B (zh) | 2007-09-07 | 2008-08-13 | 负载热气的处理方法和设备 |
AU2008298096A AU2008298096B2 (en) | 2007-09-07 | 2008-08-13 | Process and device for treating charged hot gas |
EP08785527A EP2197987A1 (de) | 2007-09-07 | 2008-08-13 | Verfahren und vorrichtung zur behandlung von beladenem heissgas |
US12/676,682 US8770555B2 (en) | 2007-09-07 | 2008-08-13 | Method and device for treating charged hot gas |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102007042543A DE102007042543A1 (de) | 2007-09-07 | 2007-09-07 | Verfahren und Vorrichtung zur Behandlung von beladenem Heißgas |
DE102007042543.2 | 2007-09-07 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2009033543A1 true WO2009033543A1 (de) | 2009-03-19 |
Family
ID=40229693
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2008/006651 WO2009033543A1 (de) | 2007-09-07 | 2008-08-13 | Verfahren und vorrichtung zur behandlung von beladenem heissgas |
Country Status (8)
Country | Link |
---|---|
US (1) | US8770555B2 (de) |
EP (1) | EP2197987A1 (de) |
CN (1) | CN101809125B (de) |
AU (1) | AU2008298096B2 (de) |
BR (1) | BRPI0816385A2 (de) |
CA (1) | CA2698909C (de) |
DE (1) | DE102007042543A1 (de) |
WO (1) | WO2009033543A1 (de) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009035051B4 (de) * | 2009-07-28 | 2011-04-21 | Uhde Gmbh | Vergasungsreaktor zur Herstellung von Rohgas |
US9085472B2 (en) * | 2010-02-26 | 2015-07-21 | General Electric Company | Gasification system employing ejectors |
AU2011298482B2 (en) * | 2010-08-30 | 2014-09-18 | Air Products And Chemicals, Inc. | Gasification reactor |
CN103232860B (zh) * | 2012-12-25 | 2014-09-03 | 杭州全合科技有限公司 | 一种高强度的气化反应器 |
CN103113926B (zh) * | 2013-02-18 | 2014-04-09 | 上海锅炉厂有限公司 | 一种高温合成气分级激冷装置及方法 |
DE102013217450A1 (de) | 2013-09-02 | 2015-03-05 | Siemens Aktiengesellschaft | Kombiniertes Quench- und Waschsystem mit Leitrohr für einen Flugstromvergasungsreaktor |
DE102013217447A1 (de) | 2013-09-02 | 2015-03-05 | Siemens Aktiengesellschaft | Kombiniertes Quench- und Waschsystem mit Innenmantel für einen Flugstromvergasungsreaktor |
DE102013217453A1 (de) | 2013-09-02 | 2015-03-05 | Siemens Aktiengesellschaft | Kombiniertes Quench- und Waschsystem mit gedoppeltem Zentralrohr für einen Flugstromvergasungsreaktor |
DE102013218839A1 (de) | 2013-09-19 | 2015-03-19 | Siemens Aktiengesellschaft | Düsendurchführung durch den Rohrschirm eines kombinierten Quench- und Waschsystems für einen Flugstromvergasungsreaktor |
DE102013218831A1 (de) | 2013-09-19 | 2015-03-19 | Siemens Aktiengesellschaft | Zentralrohr mit Oberflächenkörper eines kombinierten Quench- und Waschsystems für einen Flugstromvergasungsreaktor |
DE102013218830A1 (de) | 2013-09-19 | 2015-03-19 | Siemens Aktiengesellschaft | Geteiltes Zentralrohr eines kombinierten Quench- und Waschsystems für einen Flugstromvergasungsreaktor |
DE102014201890A1 (de) | 2014-02-03 | 2015-08-06 | Siemens Aktiengesellschaft | Kühlung und Waschung eines Rohgases aus der Flugstromvergasung |
DE102016211869A1 (de) | 2016-06-30 | 2018-01-04 | Siemens Aktiengesellschaft | Kombinierter Freiraumquench für einen Flugstromvergasungsreaktor großer Leistung mit Quench- und Waschstufe |
DE102016211870A1 (de) | 2016-06-30 | 2018-01-04 | Siemens Aktiengesellschaft | Freiraumquench für einen Flugstromvergasungsreaktor großer Leistung |
CN107537266B (zh) * | 2017-10-10 | 2023-05-05 | 北京恒丰亚业科技发展有限公司 | 一种高温热解气体的除尘系统及除尘方法 |
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US3593968A (en) * | 1968-09-26 | 1971-07-20 | Stone & Webster Eng Corp | Rapid cooling for high-temperature gas streams |
EP0084343A1 (de) * | 1982-01-20 | 1983-07-27 | Ruhrkohle Aktiengesellschaft | Quench für eine Kohlevergasungsanlage |
US4474584A (en) * | 1983-06-02 | 1984-10-02 | Texaco Development Corporation | Method of cooling and deashing |
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EP0870818A2 (de) * | 1997-04-08 | 1998-10-14 | MAN Gutehoffnungshütte Aktiengesellschaft | Synthesegaserzeuger mit Brenn- und Quenchkammer |
DE102005041930A1 (de) * | 2005-08-24 | 2007-03-01 | Future Energy Gmbh | Vergasungsverfahren und Vorrichtung zur Erzeugung von Synthesegasen durch Partialoxidation von aschehaltigen Brennstoffen unter erhöhtem Druck und Quenchkühlung des Rohgases |
DE202007011055U1 (de) * | 2007-01-16 | 2007-12-06 | IAG Industrie-Anlagen-Bau Georgsmarienhütte GmbH | Druckvergasungsreaktor |
DE102006031816A1 (de) * | 2006-07-07 | 2008-01-10 | Siemens Fuel Gasification Technology Gmbh | Verfahren und Vorrichtung zur Kühlung von heißen Gasen und verflüssigter Schlacke bei der Flugstromvergasung |
DE102007006988A1 (de) * | 2007-02-07 | 2008-08-14 | Technische Universität Bergakademie Freiberg | Verfahren und Vorrichtung zur Konvertierung von Rohgasen der Kohlevergasung |
DE102007006984A1 (de) * | 2007-02-07 | 2008-08-14 | Technische Universität Bergakademie Freiberg | Verfahren und Vorrichtung zur Konvertierung von Rohgasen bei der Flugstromvergasung |
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DE102005042640A1 (de) | 2005-09-07 | 2007-03-29 | Future Energy Gmbh | Verfahren und Vorrichtung zur Erzeugung von Synthesegasen durch Partialoxidation von aus aschehaltigen Brennstoffen erzeugten Slurries mit Teilquenchung und Abhitzegewinnung |
-
2007
- 2007-09-07 DE DE102007042543A patent/DE102007042543A1/de not_active Withdrawn
-
2008
- 2008-08-13 EP EP08785527A patent/EP2197987A1/de not_active Withdrawn
- 2008-08-13 CN CN2008801057599A patent/CN101809125B/zh active Active
- 2008-08-13 CA CA2698909A patent/CA2698909C/en active Active
- 2008-08-13 US US12/676,682 patent/US8770555B2/en active Active
- 2008-08-13 AU AU2008298096A patent/AU2008298096B2/en active Active
- 2008-08-13 WO PCT/EP2008/006651 patent/WO2009033543A1/de active Application Filing
- 2008-08-13 BR BRPI0816385-5A2A patent/BRPI0816385A2/pt not_active IP Right Cessation
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3414247A (en) * | 1966-06-07 | 1968-12-03 | Chemical Construction Corp | Synthesis gas quencher |
US3593968A (en) * | 1968-09-26 | 1971-07-20 | Stone & Webster Eng Corp | Rapid cooling for high-temperature gas streams |
EP0084343A1 (de) * | 1982-01-20 | 1983-07-27 | Ruhrkohle Aktiengesellschaft | Quench für eine Kohlevergasungsanlage |
US4605423A (en) * | 1982-04-12 | 1986-08-12 | Texaco Development Corporation | Apparatus for generating and cooling synthesis gas |
US4474584A (en) * | 1983-06-02 | 1984-10-02 | Texaco Development Corporation | Method of cooling and deashing |
EP0284762A2 (de) * | 1987-04-03 | 1988-10-05 | Deutsche Babcock Energie- und Umwelttechnik Aktiengesellschaft | Vorrichtung zum Kühlen eines Synthesegases in einem Quenchkühler |
EP0870818A2 (de) * | 1997-04-08 | 1998-10-14 | MAN Gutehoffnungshütte Aktiengesellschaft | Synthesegaserzeuger mit Brenn- und Quenchkammer |
DE102005041930A1 (de) * | 2005-08-24 | 2007-03-01 | Future Energy Gmbh | Vergasungsverfahren und Vorrichtung zur Erzeugung von Synthesegasen durch Partialoxidation von aschehaltigen Brennstoffen unter erhöhtem Druck und Quenchkühlung des Rohgases |
DE102006031816A1 (de) * | 2006-07-07 | 2008-01-10 | Siemens Fuel Gasification Technology Gmbh | Verfahren und Vorrichtung zur Kühlung von heißen Gasen und verflüssigter Schlacke bei der Flugstromvergasung |
DE202007011055U1 (de) * | 2007-01-16 | 2007-12-06 | IAG Industrie-Anlagen-Bau Georgsmarienhütte GmbH | Druckvergasungsreaktor |
DE102007006988A1 (de) * | 2007-02-07 | 2008-08-14 | Technische Universität Bergakademie Freiberg | Verfahren und Vorrichtung zur Konvertierung von Rohgasen der Kohlevergasung |
DE102007006984A1 (de) * | 2007-02-07 | 2008-08-14 | Technische Universität Bergakademie Freiberg | Verfahren und Vorrichtung zur Konvertierung von Rohgasen bei der Flugstromvergasung |
Also Published As
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AU2008298096A1 (en) | 2009-03-19 |
BRPI0816385A2 (pt) | 2015-03-03 |
US8770555B2 (en) | 2014-07-08 |
CA2698909C (en) | 2016-10-11 |
AU2008298096B2 (en) | 2014-01-23 |
CN101809125A (zh) | 2010-08-18 |
DE102007042543A1 (de) | 2009-03-12 |
US20110049256A1 (en) | 2011-03-03 |
EP2197987A1 (de) | 2010-06-23 |
CA2698909A1 (en) | 2009-03-19 |
CN101809125B (zh) | 2013-08-21 |
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