UA102077C2 - Reactor and method for flow gasification of liquid or finely comminuted solid fuel - Google Patents

Reactor and method for flow gasification of liquid or finely comminuted solid fuel

Info

Publication number
UA102077C2
UA102077C2 UAA201004481A UAA201004481A UA102077C2 UA 102077 C2 UA102077 C2 UA 102077C2 UA A201004481 A UAA201004481 A UA A201004481A UA A201004481 A UAA201004481 A UA A201004481A UA 102077 C2 UA102077 C2 UA 102077C2
Authority
UA
Ukraine
Prior art keywords
chamber
synthesis gas
reactor
liquid
liquid slag
Prior art date
Application number
UAA201004481A
Other languages
Russian (ru)
Ukrainian (uk)
Inventor
Йоханнес КОВОЛЛЬ
Эберхард КУСКЕ
Ральф АБРАХАМ
Макс Хайнритц-Адриан
Original Assignee
Тиссенкрупп Уде Гмбх
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 Тиссенкрупп Уде Гмбх filed Critical Тиссенкрупп Уде Гмбх
Priority claimed from PCT/EP2008/007841 external-priority patent/WO2009036985A1/en
Publication of UA102077C2 publication Critical patent/UA102077C2/en

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
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/48—Apparatus; Plants
    • C10J3/485—Entrained flow gasifiers
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
    • 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
    • C10J3/46—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
    • C10J3/72—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
    • 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
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/02—Processes for making hydrogen or synthesis gas
    • C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/08—Methods of heating or cooling
    • C01B2203/0872—Methods of cooling
    • C01B2203/0877—Methods of cooling by direct injection of fluid
    • 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
    • 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
    • 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
    • C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
    • C10J2300/1628—Ash post-treatment
    • C10J2300/1634—Ash vitrification

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

The invention relates to a method and a device for obtaining synthesis gas by the gasification of liquid or finely comminuted, solid fuels at a pressure of 0.3 to 8 Mpa at a temperature in the range of 1200 to 2000 °C with oxygen-containing, gaseous gasification agents in a cooled reactor (3), wherein liquid slag is deposited on the walls thereof. The reactor is located in a first pressure container. The obtained synthesis gas is generated in a first reaction chamber (2), arranged at the top of the reactor. In the upper region thereof, the substances to be used are fed. Liquid slag is deposited on the side walls thereof and can run off freely without the surface of the slag solidifying. At the bottom side thereof, an opening (6) with a dripping edge (7) is located, from where the obtained synthesis gas can be withdrawn toward the bottom and the liquid slag running down can drain. A second chamber (8) connects to the opening at the bottom, the synthesis gas being kept dry and being cooled in said second chamber (8). A water film that is produced by suitable devices and that falls freely delimits the second chamber. A third chamber (15) connects to the second chamber at the bottom and in it cooling takes place by adding water to the synthesis gas. A water bath (21) connects to the bottom of the third chamber, the drained and already solidified or still liquid slag particles dropping into said water bath. At the bottom or on the side of the third chamber (15), but above the water bath (21), the generated and cooled synthesis gas is withdrawn from the pressure container (4).
UAA201004481A 2007-09-18 2008-09-18 Reactor and method for flow gasification of liquid or finely comminuted solid fuel UA102077C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE200710044726 DE102007044726A1 (en) 2007-09-18 2007-09-18 Synthesis gas producing method, involves drying and cooling synthesis gas in chamber, arranging water bath below another chamber, and extracting produced and cooled synthesis gas from pressure container below or lateral to latter chamber
PCT/EP2008/007841 WO2009036985A1 (en) 2007-09-18 2008-09-18 Gasification reactor and method for entrained-flow gasification

Publications (1)

Publication Number Publication Date
UA102077C2 true UA102077C2 (en) 2013-06-10

Family

ID=40348667

Family Applications (1)

Application Number Title Priority Date Filing Date
UAA201004481A UA102077C2 (en) 2007-09-18 2008-09-18 Reactor and method for flow gasification of liquid or finely comminuted solid fuel

Country Status (2)

Country Link
DE (1) DE102007044726A1 (en)
UA (1) UA102077C2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2699714C (en) 2007-09-18 2016-04-19 Uhde Gmbh Gasification reactor and process for entrained-flow gasification
DE102009035052A1 (en) * 2009-07-28 2011-07-28 Uhde GmbH, 44141 Gasification reactor with double wall cooling
DE102012001986A1 (en) * 2012-02-03 2013-08-08 Thyssenkrupp Uhde Gmbh Apparatus and method for the gasification of dusty, solid, carbonaceous fuels in the flow stream
CN107129833B (en) * 2017-06-23 2024-03-29 航天长征化学工程股份有限公司 Annular pulverized coal cavity
FR3138142A1 (en) 2022-07-20 2024-01-26 IFP Energies Nouvelles IMPROVED PROCESS FOR CONVERTING A FEED CONTAINING A BIOMASS FRACTION FOR THE PRODUCTION OF FISCHER-TROPSCH SYNTHETIC HYDROCARBONS.
DE202023000387U1 (en) 2023-02-20 2023-03-28 Ralf Abraham Device for converting (CFRP & GFRP) waste into synthesis gas using an entrained flow gasifier
CN116966993B (en) * 2023-09-25 2023-11-28 包钢集团节能环保科技产业有限责任公司 Slag drying, pulverizing, crushing and separating device

Family Cites Families (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3963457A (en) 1974-11-08 1976-06-15 Koppers Company, Inc. Coal gasification process
US4247302A (en) 1979-07-13 1981-01-27 Texaco Inc. Process for gasification and production of by-product superheated steam
DE3201526A1 (en) 1982-01-20 1983-07-28 Ruhrkohle Ag, 4300 Essen "QUENCH FOR A COAL GASIFICATION PLANT"
US4474584A (en) * 1983-06-02 1984-10-02 Texaco Development Corporation Method of cooling and deashing
US4494963A (en) 1983-06-23 1985-01-22 Texaco Development Corporation Synthesis gas generation apparatus
US4704137A (en) 1987-02-09 1987-11-03 Texaco Inc. Process for upgrading water used in cooling and cleaning of raw synthesis gas
US4801306A (en) 1987-05-01 1989-01-31 Texaco Inc. Quench ring for a gasifier
DE3809313A1 (en) 1988-03-19 1989-10-05 Krupp Koppers Gmbh METHOD AND DEVICE FOR COOLING PARTIAL OXIDATION GAS
DE3824233A1 (en) 1988-07-16 1990-01-18 Krupp Koppers Gmbh PLANT FOR THE PRODUCTION OF A PRODUCT GAS FROM A FINE-PARTIC CARBON SUPPORT
DD280975B3 (en) 1989-03-31 1993-03-04 Noell Dbi Energie Entsorgung METHOD AND DEVICE FOR COOLING AND CLEANING GASES LOADED WITH SLUDGE OR DUST
GB8912316D0 (en) 1989-05-30 1989-07-12 Shell Int Research Coal gasification reactor
US4992081A (en) 1989-09-15 1991-02-12 Texaco Inc. Reactor dip tube cooling system
EP0616022B1 (en) 1993-03-16 1995-09-13 Krupp Koppers GmbH Process for pressure gasification of fine particulate fuels
US5358696A (en) 1993-12-01 1994-10-25 Texaco Inc. Production of H2 -rich gas
DE19714376C1 (en) 1997-04-08 1999-01-21 Gutehoffnungshuette Man Synthesis gas generator with combustion and quench chamber
DE19718131C2 (en) 1997-04-29 1999-10-14 Krc Umwelttechnik Gmbh Method and device for the regeneration of a liquid obtained in the power process for the digestion of wood by gasification
DE19751889C1 (en) 1997-11-22 1999-05-06 Schwarze Pumpe Energiewerke Ag Autothermal gasification of liquid waste
DE202005021666U1 (en) 2005-08-24 2009-05-20 Siemens Aktiengesellschaft Device for generating synthesis gases by partial oxidation of ash-containing fuels under elevated pressure and quench cooling of the raw gas
DE102005041931B4 (en) 2005-09-03 2018-07-05 Siemens Aktiengesellschaft Apparatus for producing synthesis gases by partial oxidation of ash-containing fuels under elevated pressure with partial quenching of the raw gas and waste heat recovery
DE102005043212A1 (en) * 2005-09-09 2007-03-15 Future Energy Gmbh Solid fuel, e.g. anthracite or gasification, for e.g. fluidized bed reactor, involves taking water-washed raw gas for deposition of particulate matters of partial condensation, where raw gas is indirectly cooled at preset temperature
DE202005021659U1 (en) 2005-10-07 2010-01-14 Siemens Aktiengesellschaft Device for high-flow entrainment gasifier

Also Published As

Publication number Publication date
DE102007044726A1 (en) 2009-03-19

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