EP0431266A1 - Procédé et appareil pour la gaséification de combustibles finement divisés à poudreux - Google Patents

Procédé et appareil pour la gaséification de combustibles finement divisés à poudreux Download PDF

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Publication number
EP0431266A1
EP0431266A1 EP90117263A EP90117263A EP0431266A1 EP 0431266 A1 EP0431266 A1 EP 0431266A1 EP 90117263 A EP90117263 A EP 90117263A EP 90117263 A EP90117263 A EP 90117263A EP 0431266 A1 EP0431266 A1 EP 0431266A1
Authority
EP
European Patent Office
Prior art keywords
gasification
reactor
burners
level
gasification reactor
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.)
Withdrawn
Application number
EP90117263A
Other languages
German (de)
English (en)
Inventor
Frank Dziobek
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.)
Krupp Koppers GmbH
Original Assignee
Krupp Koppers 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 Krupp Koppers GmbH filed Critical Krupp Koppers GmbH
Publication of EP0431266A1 publication Critical patent/EP0431266A1/fr
Withdrawn legal-status Critical Current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
    • 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
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/50—Fuel charging devices
    • C10J3/506—Fuel charging 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
    • C10J2200/00—Details of gasification apparatus
    • C10J2200/15—Details of feeding means
    • C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions

Definitions

  • the method used to achieve this object is characterized in that the gasification takes place simultaneously in two or more levels of the gasification reactor, with all gasification burners of the gasification reactor being operated under the same conditions.
  • the method according to the invention differs fundamentally in that the gasification burners are operated at all levels under the same conditions. This means that the same fuel is used and the reaction conditions for the gasification are the same for all gasification burners, whereby, of course, slight deviations between the individual gasification burners are possible due to the process.
  • the number of levels in the gasification reactor which can of course be more than two, depends primarily on the desired throughput and the spatial conditions in the overall system. It should be taken into account here that the height of the gasification reactor increases with the number of levels.
  • the gasification burners are arranged in two levels according to the invention, two gasification burners being provided on each level, which, as shown in the figures, are arranged offset by 90 ° to one another, the result is the following when the gasification reactor is twice the height:

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Combustion Of Fluid Fuel (AREA)
EP90117263A 1989-11-04 1990-09-07 Procédé et appareil pour la gaséification de combustibles finement divisés à poudreux Withdrawn EP0431266A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3936732A DE3936732A1 (de) 1989-11-04 1989-11-04 Verfahren und vorrichtung zur vergasung von feinkoernigen bis staubfoermigen brennstoffen
DE3936732 1989-11-04

Publications (1)

Publication Number Publication Date
EP0431266A1 true EP0431266A1 (fr) 1991-06-12

Family

ID=6392855

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90117263A Withdrawn EP0431266A1 (fr) 1989-11-04 1990-09-07 Procédé et appareil pour la gaséification de combustibles finement divisés à poudreux

Country Status (5)

Country Link
EP (1) EP0431266A1 (fr)
CN (1) CN1024677C (fr)
DE (1) DE3936732A1 (fr)
PL (1) PL164262B1 (fr)
ZA (1) ZA907594B (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008015801A1 (de) 2008-03-27 2009-10-01 Uhde Gmbh Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum
WO2009118082A2 (fr) 2008-03-27 2009-10-01 Uhde Gmbh Dispositif de production de gaz de synthèse présentant un réacteur de gazéification à chambre de trempe connectée
DE102008057410A1 (de) 2008-11-14 2010-05-20 Uhde Gmbh Vorrichtung zur Herstelllung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum
DE102009005464A1 (de) 2009-01-21 2010-08-05 Uhde Gmbh Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungreaktor mit anschließendem Quenchraum
US9139699B2 (en) 2012-10-04 2015-09-22 Dow Corning Corporation Metal containing condensation reaction catalysts, methods for preparing the catalysts, and compositions containing the catalysts

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2104801B1 (fr) * 2007-01-17 2016-06-22 Shell Internationale Research Maatschappij B.V. Brûleur haute capacité

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0050863A1 (fr) * 1980-10-24 1982-05-05 Hitachi, Ltd. Procédé et appareil pour gazéifier des charbons
DE3509221A1 (de) * 1984-03-16 1985-09-19 Shell Internationale Research Maatschappij B.V., Den Haag Vorrichtung fuer die vergasung eines pulverisierten festen brennstoffes

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59176391A (ja) * 1983-03-28 1984-10-05 Hitachi Ltd 石炭ガス化炉
GB2164951A (en) * 1984-09-26 1986-04-03 Shell Int Research Method and apparatus for producing synthesis gas
CN1010028B (zh) * 1985-05-29 1990-10-17 国际壳牌研究有限公司 褐煤气化器
JPH06232185A (ja) * 1993-02-05 1994-08-19 Toshiba Corp 半導体チップの仮固定方法

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0050863A1 (fr) * 1980-10-24 1982-05-05 Hitachi, Ltd. Procédé et appareil pour gazéifier des charbons
DE3509221A1 (de) * 1984-03-16 1985-09-19 Shell Internationale Research Maatschappij B.V., Den Haag Vorrichtung fuer die vergasung eines pulverisierten festen brennstoffes

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008015801A1 (de) 2008-03-27 2009-10-01 Uhde Gmbh Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum
WO2009118082A2 (fr) 2008-03-27 2009-10-01 Uhde Gmbh Dispositif de production de gaz de synthèse présentant un réacteur de gazéification à chambre de trempe connectée
US8562698B2 (en) 2008-03-27 2013-10-22 Thyssenkrupp Uhde Gmbh Device for production of synthesis gas with a gasification reactor with a subsequent quenching space
DE102008015801B4 (de) 2008-03-27 2019-02-28 Thyssenkrupp Industrial Solutions Ag Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum
DE102008057410A1 (de) 2008-11-14 2010-05-20 Uhde Gmbh Vorrichtung zur Herstelllung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum
DE102008057410B4 (de) 2008-11-14 2019-07-04 Thyssenkrupp Industrial Solutions Ag Vorrichtung zur Herstelllung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum
DE102009005464A1 (de) 2009-01-21 2010-08-05 Uhde Gmbh Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungreaktor mit anschließendem Quenchraum
US9469799B2 (en) 2011-10-04 2016-10-18 Dow Corning Corporation Metal containing condensation reaction catalysts, methods for preparing the catalysts, and compositions containing the catalysts
US9139699B2 (en) 2012-10-04 2015-09-22 Dow Corning Corporation Metal containing condensation reaction catalysts, methods for preparing the catalysts, and compositions containing the catalysts

Also Published As

Publication number Publication date
PL286915A1 (en) 1991-09-23
PL164262B1 (pl) 1994-07-29
DE3936732A1 (de) 1991-05-08
CN1024677C (zh) 1994-05-25
CN1051581A (zh) 1991-05-22
ZA907594B (en) 1991-07-31

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