DE102009039749A1 - Process for the production of synthesis gas - Google Patents
Process for the production of synthesis gas Download PDFInfo
- Publication number
- DE102009039749A1 DE102009039749A1 DE102009039749A DE102009039749A DE102009039749A1 DE 102009039749 A1 DE102009039749 A1 DE 102009039749A1 DE 102009039749 A DE102009039749 A DE 102009039749A DE 102009039749 A DE102009039749 A DE 102009039749A DE 102009039749 A1 DE102009039749 A1 DE 102009039749A1
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- Prior art keywords
- boiler
- synthesis gas
- waste heat
- radiation
- production
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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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/52—Ash-removing devices
- C10J3/526—Ash-removing devices for entrained flow 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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/485—Entrained flow 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
- C10J3/72—Other features
- C10J3/74—Construction of shells or jackets
- C10J3/76—Water jackets; Steam boiler-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
- C10J3/82—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
- C10J3/72—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
- 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
- C10K1/08—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
- C10J2200/00—Details of gasification apparatus
- C10J2200/09—Mechanical details of gasifiers not otherwise provided for, e.g. sealing means
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0075—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for syngas or cracked gas cooling systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0077—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for tempering, e.g. with cooling or heating circuits for temperature control of elements
- F28D2021/0078—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for tempering, e.g. with cooling or heating circuits for temperature control of elements in the form of cooling walls
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
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)
- Processing Of Solid Wastes (AREA)
Abstract
Mit einem Verfahren zur Herstellung von Synthesegas durch Vergasung von aschehaltigem Brennstoff mit sauerstoffhaltigem Gas bei Temperaturen oberhalb der Schmelztemperatur der Asche und einem Druck von 0,3 bis 8 MPa soll die, durch die Herstellung des Synthesegases anfallende Enthalpie für die Erzeugung von Dampf, insbesondere Hochdruckdampf, benutzt werden. Dies wird dadurch erreicht, dass das den Vergaseraustritt verlassende Mediengemisch innerhalb des Druckbehälters einen als Abhitzekessel gestalteten Bereich in Schwerkraftrichtung nach unten durchströmt, wobei das Synthesegas auf eine Austrittstemperatur von 200°C bis 400°C abgekühlt wird.With a process for the production of synthesis gas by gasifying ash-containing fuel with oxygen-containing gas at temperatures above the melting temperature of the ash and a pressure of 0.3 to 8 MPa, the enthalpy resulting from the production of the synthesis gas for the generation of steam, especially high-pressure steam , to be used. This is achieved in that the media mixture leaving the gasifier outlet flows downwards in the direction of gravity through an area designed as a waste heat boiler inside the pressure vessel, the synthesis gas being cooled to an outlet temperature of 200 ° C to 400 ° C.
Description
Die Erfindung richtet sich auf ein Verfahren zur Herstellung von Synthesegas durch Vergasung von aschehaltigem Brennstoff mit sauerstoffhaltigem Gas bei Temperaturen oberhalb der Schmelztemperatur der Asche und einem Druck von 0,3 bis 8 MPa.The invention is directed to a process for the production of synthesis gas by gasification of ash-containing fuel with oxygen-containing gas at temperatures above the melting temperature of the ash and a pressure of 0.3 to 8 MPa.
Derartige Vergasungsverfahren und entsprechende Reaktoren sind in unterschiedlichen Bauweisen bekannt, lediglich als Beispiel sei hier auf die
Bei der Vergasung deratiger kohlenstoffhaltiger Brennstoffe kommen beispielsweise Kohlen, Koks, Petrolkoks, Biomasse oder dergleichen zum Einsatz, wobei hier die Flugstromvergasung vorgesehen sein kann, mit Trockeneinspeisen des Vergaserfeeds zur Erzeugung von Kraftstoffen, Chemierohstoffen aber auch zur Erzeugung von Energie.In the gasification of deratiger carbonaceous fuels such as coal, coke, petroleum coke, biomass or the like are used, here the entrained flow gasification can be provided with Trockeneinspeisen the carburetor feed for the production of fuels, chemical raw materials but also for the production of energy.
Hier setzt die Erfindung an, deren Aufgabe darin besteht, die durch die Herstellung des Synthesegases anfallenden Enthalpie für die Erzeugung von Dampf, insbesondere Hochdruckdampf zu benutzen.This is where the invention begins, the object of which is to use the enthalpy produced by the production of the synthesis gas for the production of steam, in particular high-pressure steam.
Diese Aufgabe wird mit einem Verfahren der eingangs bezeichneten Art dadurch gelöst, dass das den Vergaseraustritt verlassene Mediengemisch innerhalb des Druckbehälters einen als Abhitzekessel gestaltenden Bereich in Schwerkraftrichtung nach unten durchströmt, wobei das Synthesegas auf eine Austrittstemperatur von 200°C bis 400°C abgekühlt wird.This object is achieved by a method of the type described above in that the leaving the carburetor leaving media mixture within the pressure vessel designed as a waste heat boiler area flows in the direction of gravity down, the synthesis gas is cooled to an outlet temperature of 200 ° C to 400 ° C.
Durch die erfindungsgemäße Verfahrensweise ist es möglich durch den dem Flugstromvergaser nachgeschalteten Abhitzekesselbereich, die im Mediengemisch enthaltene Wärme und Enthalpie zu nutzen, um Dampf oder ein Wasserdampfgemisch zu erzeugen, das einer weiteren Verwendung zuführbar ist. Mit dem Ausdruck ”Mediengemisch” ist insbesondere das Synthesegas und die weiteren Bestandteile, wie z. B. die Schlacke und dergleichen gemeint.By means of the procedure according to the invention, it is possible to utilize the heat and enthalpy contained in the media mixture by means of the waste-heat boiler area connected downstream of the entrained-flow gasifier in order to produce steam or a steam mixture which can be fed to a further use. With the term "media mixture" in particular the synthesis gas and the other ingredients, such as. For example, the slag and the like are meant.
Weitere Ausgestaltungen der Erfindung ergeben sich aus den Unteransprüchen, dabei kann insbesondere vorgesehen sein, dass das Mediengemisch (Synthesegas) nach dem Vergaseraustritt und vor dem Eintritt in den Abhitzekesselbereich von einem Wasserquench beaufschlagt wird. In einem solchen Fall kann das heiße Rohsynthesegas von der Vergasertemperatur von ca. 1300°C bis 1600°C durch einen Wasserquench auf ca. 900°C abgekühlt werden, wobei das Mediengemisch dann innerhalb des Abhitzekesselbereiches auf eine Temperatur von 300°C bis 400°C abkühlbar ist.Further embodiments of the invention will become apparent from the dependent claims, it can be provided in particular that the media mixture (synthesis gas) is acted upon by the gas outlet and before entering the waste heat boiler area of a water quench. In such a case, the hot raw synthesis gas can be cooled from the carburetor temperature of about 1300 ° C to 1600 ° C by a water quench to about 900 ° C, wherein the media mixture then within the waste heat boiler range to a temperature of 300 ° C to 400 ° C is coolable.
Ein abgewandeltes Ausführungsbeispiel der Erfindung besteht darin, dass das Mediengemisch (Synthesegas) hinter dem Abhitzekesselbereich von einem Wasserquench beaufschlagt ist. Hier wird das heiße Synthesegas im Abhitzekesselbereich von ca. 1300°C bis 1600°C auf 800°C bis 900°C entsprechend abgekühlt und anschließend durch einen Wasserquench auf 200°C bis 300°C weiter abgekühlt.A modified embodiment of the invention is that the media mixture (synthesis gas) behind the waste heat boiler area is acted upon by a water quench. Here, the hot synthesis gas is cooled in the waste heat boiler range of about 1300 ° C to 1600 ° C to 800 ° C to 900 ° C and then further cooled by a water quench at 200 ° C to 300 ° C.
Zur Lösung der eingangsformulierten Aufgabe sieht die Erfindung auch eine Vorrichtung zur Herstellung von Synthesegas vor, die sich dadurch auszeichnet, dass hinter dem Vergaser im Druckbehälter eine im Abhitzekesselbereich bildende Strahlungskesselwand aus Kesselspeisewasser durchströmten Rohren vorgesehen ist.To solve the above-described problem, the invention also provides an apparatus for the production of synthesis gas, which is characterized in that behind the carburetor in the pressure vessel a forming in the waste heat boiler area radiation boiler wall from boiler feed water flowed through pipes is provided.
In Ausgestaltung einer derartigen Vorrichtung kann auch vorgesehen sein, dass die Kesselstrahlungswand Kesselspeisewasser durchströmte, in das Reaktorinnere ragende Schotten aufweist.In an embodiment of such a device can also be provided that the boiler radiation wall flowed through boiler feed water, having projecting into the interior of the reactor bulkheads.
Durch die Quenchung von 1300°C bis 1600°C hinunter auf 900°C werden die glutflüssigen Aschepartikel verfestigt, so dass in dem nachgeschalteten Abhitzekessel die Dampferzeugung ohne feste unlösbare Anbackungen ermöglicht wird, da der dann fest vorliegende Flugstaub entweder nicht an den Wärmetauscherflächen anhaftet oder leicht über Klopfer oder Rußbläser abgereinigt werden kann.By quenching from 1300 ° C to 1600 ° C down to 900 ° C, the glutinous ash particles are solidified, so that in the downstream heat recovery steam generator without fixed insoluble caking is possible because the solid dust present then either does not adhere to the heat exchanger surfaces or can be easily cleaned by knocker or sootblower.
Wie schon oben ausgeführt, wird in dem Abhitzekesselbereich, der aus einer Strahlungskesselwand und aus in den Gasstrom ragenden Schotten (beide in Rohr-Steg-Rohr-Ausführung) gebildet ist, wobei die Schotten nur etwa bis zu einem Drittel in den Kessel hineinragen, das Synthesegas nach der Wasserquenchung von ca. 900°C auf unter 400°C abgekühlt, wobei mit dieser Enthalpie Dampf, in Kraftwerksprozess bevorzugt Hochdruckdampf, bei einer Synthesegasherstellung bevorzugt Mitteldruckdampf, erzeugt wird. Das nach der Wasserquenchung mit folgender Abkühlung mit Dampf beladene, teilgesättige Synthesegas wird dann aus dem Abhitzekessel weiteren Behandlungsschritten zugeführt.As already stated above, in the waste-heat boiler zone, which consists of a radiation boiler wall and bulkheads projecting into the gas flow (both in pipe-web-pipe design), the bulkheads projecting into the boiler only up to one third Synthesis gas after quenching of water from about 900 ° C to below 400 ° C cooled, with this enthalpy steam, in power plant process preferably high pressure steam, in a syngas production preferably medium-pressure steam, is generated. The after-water quenching with the following cooling with steam laden, partially saturated synthesis gas is then supplied from the waste heat boiler further treatment steps.
Alternativ ist eine erfindungsgemäße Vorrichtung vorgesehen, bei der vor und/oder nach der Kesselstrahlungswand in Strömungsrichtung der Medien ein Wasserquench vorgesehen ist, wobei, wie oben schon angegeben, erfindungsgemäß die entsprechenden Wandflächen und die Schotten von einer Rohr-Steg-Rohrkonstruktion gebildet sind, darüber hinaus können, wie ebenfalls oben schon angegeben, Klopfer und/oder Rußbläser zur Abreinigung der jeweiligen Wandflächen vorgesehen sein.Alternatively, a device according to the invention is provided, in which before and / or after the boiler radiation wall in the flow direction of the media a water quench is provided, wherein, as already stated above, according to the invention, the corresponding wall surfaces and the bulkheads are formed by a pipe-web pipe construction, above In addition, as already stated above, knockers and / or sootblowers can be provided for cleaning off the respective wall surfaces.
Wird der Wasserquench, wie dies die Erfindung ebenfalls vorsieht, erst hinter dem Abhitzekesselbereich positioniert, wird auch hier das Synthesegas mit Wasserdampf teilweise aufgesättigt, wobei der Strahlungskessel in Strömungsrichtung unterhalb des Vergasers erfindungsgemäß so dimensioniert ist, dass das heiße Synthesegas vorwiegend über Strahlungswärmeabgabe gekühlt wird und der Strahlungskessel ebenfalls aus einer in dem Druckbehälter befindlichen Strahlungskesselwand mit in den Gasstrom ragenden Schotten besteht.If the water quench, as the invention also provides, is positioned only behind the waste heat boiler area, the synthesis gas is also partially saturated with water vapor, with the radiation boiler in the flow direction is dimensioned according to the invention below the carburetor so that the hot synthesis gas is mainly cooled by radiant heat and the radiation boiler also consists of a located in the pressure vessel radiation boiler wall projecting into the gas flow bulkheads.
Erkennbar können die beiden erfindungsgemäßen Varianten sowohl das entsprechende Verfahren, wie die entsprechende Vorrichtung, zur Optimierung der Vergasung für Kraftwerksprozesse eingesetzt werden, wobei auch eine möglichst effiziente Rohstoffnutzung bei der Herstellung von Synthesegasen, wie CO oder H2 für die chemische Industrie und die Herstellung synthetischer Kraftstoffe oder synthetisches Erdgases und für Anlagen zur kombinierten Erzeugung von Strom und Herstellung von Chemikalien (Polygeneration) eingesetzt werden können.The two variants according to the invention can be used both for the corresponding method and the corresponding device for optimizing the gasification for power plant processes, whereby the most efficient use of raw materials in the production of synthesis gases, such as CO or H 2 for the chemical industry and the production of synthetic Fuels or synthetic natural gas and for plants for the combined generation of electricity and production of chemicals (polygeneration) can be used.
Weitere Merkmale, Einzelheiten und Vorteile der Erfindung ergeben sich aufgrund der nachfolgenden Beschreibung sowie anhand der Zeichnung, diese zeigt in denOther features, objects and advantages of the invention will become apparent from the following description and from the drawing, which shows in the
Die allgemein mit
Der Reaktionsraum
Der Abhitzekesselbereich C ist als Strahlungskessel
Am unteren Ende ist ein Schlackesammelbehälter
Zusätzlich sind in
Erkennbar kann die Gesamtenthalpie des den Reaktor
In
Im Unterschied zur Konstruktion nach
Natürlich sind die beschriebenen Ausführungsbeispiele der Erfindung noch in vielfacher Hinsicht abzuändern ohne den Grundgedanken zu verlassen, insbesondere was die Führung der in Schwerkraftrichtung von oben nach unten strömenden Medien innerhalb des Reaktors
ZITATE ENTHALTEN IN DER BESCHREIBUNG QUOTES INCLUDE IN THE DESCRIPTION
Diese Liste der vom Anmelder aufgeführten Dokumente wurde automatisiert erzeugt und ist ausschließlich zur besseren Information des Lesers aufgenommen. Die Liste ist nicht Bestandteil der deutschen Patent- bzw. Gebrauchsmusteranmeldung. Das DPMA übernimmt keinerlei Haftung für etwaige Fehler oder Auslassungen.This list of the documents listed by the applicant has been generated automatically and is included solely for the better information of the reader. The list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions.
Zitierte PatentliteraturCited patent literature
- WO 2009/036985 A1 [0002] WO 2009/036985 A1 [0002]
Claims (8)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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DE102009039749A DE102009039749A1 (en) | 2009-09-02 | 2009-09-02 | Process for the production of synthesis gas |
PCT/EP2010/005253 WO2011026589A2 (en) | 2009-09-02 | 2010-08-27 | Method for producing synthetic gas |
EP10749789A EP2531574A2 (en) | 2009-09-02 | 2010-08-27 | Method for producing synthetic gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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DE102009039749A DE102009039749A1 (en) | 2009-09-02 | 2009-09-02 | Process for the production of synthesis gas |
Publications (1)
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DE102009039749A1 true DE102009039749A1 (en) | 2011-03-10 |
Family
ID=43536030
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DE102009039749A Withdrawn DE102009039749A1 (en) | 2009-09-02 | 2009-09-02 | Process for the production of synthesis gas |
Country Status (3)
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EP (1) | EP2531574A2 (en) |
DE (1) | DE102009039749A1 (en) |
WO (1) | WO2011026589A2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012136451A1 (en) * | 2011-04-05 | 2012-10-11 | Siemens Aktiengesellschaft | Device for producing synthesis gas |
WO2013007341A1 (en) * | 2011-07-14 | 2013-01-17 | Thyssenkrupp Uhde Gmbh | Apparatus and method for introducing renewable fuels into the region of the radiation boiler wall of gasification reactors |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN102796570B (en) * | 2011-12-28 | 2014-11-12 | 上海锅炉厂有限公司 | Novel composite type high-temperature raw gas cooling and washing equipment |
Citations (2)
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DE102005048488A1 (en) * | 2005-10-07 | 2007-05-03 | Future Energy Gmbh | Method and apparatus for high power airstream gasifier |
WO2009036985A1 (en) | 2007-09-18 | 2009-03-26 | Uhde Gmbh | Gasification reactor and method for entrained-flow gasification |
Family Cites Families (6)
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DE3725424C1 (en) * | 1987-07-31 | 1988-07-21 | Steinmueller Gmbh L & C | Radiation cooler for cooling gases laden with dust |
DK164245C (en) * | 1990-01-05 | 1992-10-26 | Burmeister & Wains Energi | GAS COOLERS FOR HEAT TRANSMISSION BY RADIATION |
JP4933442B2 (en) * | 2004-11-22 | 2012-05-16 | シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ | Fuel gasifier |
US8684070B2 (en) * | 2006-08-15 | 2014-04-01 | Babcock & Wilcox Power Generation Group, Inc. | Compact radial platen arrangement for radiant syngas cooler |
US9051522B2 (en) * | 2006-12-01 | 2015-06-09 | Shell Oil Company | Gasification reactor |
US7670574B2 (en) * | 2007-01-19 | 2010-03-02 | General Electric Company | Methods and apparatus to facilitate cooling syngas in a gasifier |
-
2009
- 2009-09-02 DE DE102009039749A patent/DE102009039749A1/en not_active Withdrawn
-
2010
- 2010-08-27 WO PCT/EP2010/005253 patent/WO2011026589A2/en active Application Filing
- 2010-08-27 EP EP10749789A patent/EP2531574A2/en not_active Withdrawn
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005048488A1 (en) * | 2005-10-07 | 2007-05-03 | Future Energy Gmbh | Method and apparatus for high power airstream gasifier |
WO2009036985A1 (en) | 2007-09-18 | 2009-03-26 | Uhde Gmbh | Gasification reactor and method for entrained-flow gasification |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012136451A1 (en) * | 2011-04-05 | 2012-10-11 | Siemens Aktiengesellschaft | Device for producing synthesis gas |
WO2013007341A1 (en) * | 2011-07-14 | 2013-01-17 | Thyssenkrupp Uhde Gmbh | Apparatus and method for introducing renewable fuels into the region of the radiation boiler wall of gasification reactors |
DE102011107726A1 (en) * | 2011-07-14 | 2013-01-17 | Thyssenkrupp Uhde Gmbh | Apparatus and method for introducing renewable fuels into the region of the radiation vessel wall of gasification reactors |
DE102011107726B4 (en) * | 2011-07-14 | 2016-06-30 | Thyssenkrupp Industrial Solutions Ag | Apparatus and method for introducing renewable fuels into the region of the radiation vessel wall of gasification reactors |
Also Published As
Publication number | Publication date |
---|---|
WO2011026589A2 (en) | 2011-03-10 |
WO2011026589A3 (en) | 2011-07-21 |
EP2531574A2 (en) | 2012-12-12 |
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