KR850004259A - 탄화수소연료로 부터 합성가스를 제조하는 방법 - Google Patents

탄화수소연료로 부터 합성가스를 제조하는 방법 Download PDF

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Publication number
KR850004259A
KR850004259A KR1019840007693A KR840007693A KR850004259A KR 850004259 A KR850004259 A KR 850004259A KR 1019840007693 A KR1019840007693 A KR 1019840007693A KR 840007693 A KR840007693 A KR 840007693A KR 850004259 A KR850004259 A KR 850004259A
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South Korea
Prior art keywords
oxidant
hydrocarbon fuel
gas
sec
slow
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KR1019840007693A
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KR920000778B1 (ko
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요하누스 안토니우스 하세나크 헨드리쿠스
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안토니우스 토니스 푸이슈터
셀 인터나 쵸나아레 레사아치 마아츠샤피 비이부이
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    • 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
    • C01B3/363—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 characterised by the burner used
    • 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
    • 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
    • C10J2300/0926—Slurries comprising bio-oil or bio-coke, i.e. charcoal, obtained, e.g. by fast pyrolysis of 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
    • C10J2300/12—Heating the gasifier
    • C10J2300/1223—Heating the gasifier by burners
    • 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
    • Y02P20/141—Feedstock
    • Y02P20/145—Feedstock the feedstock being materials of biological origin

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

내용 없음

Description

탄화수소연료로 부터 합성가스를 제조하는 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 본 발명의 방법에 사용되는 첫번째 버너의 종단면이다. 제2도는 본 발명의 방법에 사용되는 두번째 버너의 종단면도이다.

Claims (10)

  1. 하나 또는 그 이상의 버너의 제2환형배출로, 제1 환형배출로 및 중앙배출로를 통해 각기 저속 탄화 수소연료, 고속산화제류 및 저속산화제류를 반응대역내 도입시켜 탄화수소연료가 산화제와 반응되게 하는 것으로 구성된 액체상태 또는 슬러리상태의 탄화수소연료를 산소 또는 산소함유 기체로 구성된 산화제를 사용하여 부분연소함으로써 합성가스를 제조하는 방법.
  2. 제1항에 있어서, 탄화수소 연료류를 반응대역내 도입시키기에 앞서 분쇄작용을 가진 매체와 혼합해주는 방법.
  3. 제1항 또는 제2항에 있어서, 탄화수소연료류를 약 5-15m/초의 속도로 반응대역내 도입시키는 방법.
  4. 제1항 내지 제3항중 어느 하나에서 고속산화제와 저속산화제의 질량흐름비가 약30:70인 방법.
  5. 제1항 내지 제4항중 어느 하나에서 고속산화제류가 버너로 부터 약 50-90m/초의 속도로 유출되는 방법.
  6. 제1항 내지 제5항중 어느 하나에서 저속산화제류가 버너로 부터 약 10-30m/초의 속도로 유출되는 방법.
  7. 제1항 내지 제6항중 어느 하나에서 저속의 감속 기체류가 산화제와 연료류의 둘레에 형성된 방법.
  8. 제7항에 있어서, 감속기체가중기, 이산화탄소, 질소 냉각 반응기기체 또는 그 혼합물로 형성되어 있는 방법.
  9. 제7항 또는 제8항에 있어서, 감속기체류가 버너(들)로 부너 나올때 약 10-40m/초의 속도를 갖는 방법.
  10. 첨부도면들을 특별참조로 하여 설명한 바와 같이 액체상태 또는 슬러리상태의 탄화수소연료를 부분연소하여 합성가스를 제조하는 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019840007693A 1983-12-09 1984-12-06 탄화수소연료로부터 합성가스를 제조하는 방법 KR920000778B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB08332945A GB2151348B (en) 1983-12-09 1983-12-09 Burner and process for producing synthesis gas from hydrocarbon fuel
GB32945 1983-12-09

Publications (2)

Publication Number Publication Date
KR850004259A true KR850004259A (ko) 1985-07-11
KR920000778B1 KR920000778B1 (ko) 1992-01-23

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019840007693A KR920000778B1 (ko) 1983-12-09 1984-12-06 탄화수소연료로부터 합성가스를 제조하는 방법

Country Status (12)

Country Link
JP (1) JPH0694361B2 (ko)
KR (1) KR920000778B1 (ko)
CN (1) CN85105729A (ko)
BR (1) BR8406227A (ko)
CA (1) CA1269842A (ko)
CS (1) CS269965B2 (ko)
DD (1) DD229982A5 (ko)
DE (1) DE3444590C2 (ko)
ES (1) ES8507418A1 (ko)
FR (1) FR2556332B1 (ko)
GB (1) GB2151348B (ko)
PT (1) PT79633B (ko)

Families Citing this family (20)

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GB8619076D0 (en) * 1986-08-05 1986-09-17 Shell Int Research Partial oxidation of fuel
GB8711156D0 (en) * 1987-05-12 1987-06-17 Shell Int Research Partial oxidation of hydrocarbon-containing fuel
US4887962A (en) * 1988-02-17 1989-12-19 Shell Oil Company Partial combustion burner with spiral-flow cooled face
US4865542A (en) * 1988-02-17 1989-09-12 Shell Oil Company Partial combustion burner with spiral-flow cooled face
JP2928299B2 (ja) * 1989-09-22 1999-08-03 株式会社神戸製鋼所 還元ガスの発生方法
ES2120207T3 (es) * 1994-05-19 1998-10-16 Shell Int Research Un procedimiento para la fabricacion de gas de sintesis por oxidacion parcial de un combustible que contiene hidrocarburo liquido empleando un quemador (co-anular) de multi-orificios.
AT402440B (de) * 1995-06-01 1997-05-26 Voest Alpine Ind Anlagen Brenner
ATE262483T1 (de) * 1998-10-30 2004-04-15 Casale Chemicals Sa Verfahren und brenner für die teiloxidation von kohlenwasserstoffen
DE19941978B4 (de) * 1999-09-03 2005-09-22 Stiebel Eltron Gmbh & Co. Kg Verfahren und Einrichtung zur Erzeugung eines Synthesegases
DE20001421U1 (de) 2000-01-27 2000-05-11 Noell-KRC Energie- und Umwelttechnik GmbH, 04435 Schkeuditz Vorrichtung zur Vergasung von homogenen Brenn-, Rest- und Abfallstoffen
JP4851027B2 (ja) * 2001-06-22 2012-01-11 大陽日酸株式会社 一酸化炭素、水素生成用燃焼装置及びバーナ
DE10248530B4 (de) * 2002-10-14 2004-08-12 Thermoselect Ag Sauerstofflanze zur Hochtemperaturvergasung von Abfällen, sowie Verfahren zum Betreiben derselben
DK1607370T3 (da) * 2004-06-18 2011-11-21 Casale Chemicals Sa Fremgangsmåde og brænder til delvis oxidation af carbonhydrider
JP4739090B2 (ja) * 2006-04-06 2011-08-03 大陽日酸株式会社 バーナ又はランスの冷却構造
CN101363626B (zh) * 2007-08-06 2015-05-20 国际壳牌研究有限公司 制造燃烧器前脸的方法
CN101363624B (zh) 2007-08-06 2011-05-25 国际壳牌研究有限公司 燃烧器
CN202835334U (zh) * 2012-04-02 2013-03-27 国际壳牌研究有限公司 用于气化固体燃料的燃烧器
CN104560210A (zh) * 2015-01-19 2015-04-29 清华大学 水煤浆雾化喷嘴和具有水煤浆雾化喷嘴的气化炉
RU2640079C2 (ru) * 2016-06-16 2017-12-26 Алексей Александрович Никифоров Химический реактор сжатия
CN114231320B (zh) * 2021-11-29 2023-04-14 北京航化节能环保技术有限公司 一种可变负荷运行的煤气化装置

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GB1266072A (ko) * 1969-02-11 1972-03-08
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FR2230583A1 (en) * 1973-05-24 1974-12-20 Texaco Development Corp Synthesis gas generation - using triple orifice burner designed to prevent heat induced damage
JPS5246192A (en) * 1975-10-11 1977-04-12 Hideo Furukawa Discharge printing method and apparatus
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Also Published As

Publication number Publication date
GB2151348B (en) 1986-08-06
CS269965B2 (en) 1990-05-14
PT79633A (en) 1985-01-01
DE3444590A1 (de) 1985-06-20
CA1269842A (en) 1990-06-05
DE3444590C2 (de) 1996-02-29
FR2556332B1 (fr) 1988-10-21
CS945184A2 (en) 1989-10-13
GB2151348A (en) 1985-07-17
DD229982A5 (de) 1985-11-20
CN85105729A (zh) 1987-03-04
GB8332945D0 (en) 1984-01-18
ES538324A0 (es) 1985-09-01
KR920000778B1 (ko) 1992-01-23
JPS60141602A (ja) 1985-07-26
FR2556332A1 (fr) 1985-06-14
PT79633B (en) 1986-10-21
JPH0694361B2 (ja) 1994-11-24
ES8507418A1 (es) 1985-09-01
BR8406227A (pt) 1985-10-01

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