JPS63240941A - 気相下の被酸化性原料の酸化方法とこの方法を実施する反応器 - Google Patents

気相下の被酸化性原料の酸化方法とこの方法を実施する反応器

Info

Publication number
JPS63240941A
JPS63240941A JP61308989A JP30898986A JPS63240941A JP S63240941 A JPS63240941 A JP S63240941A JP 61308989 A JP61308989 A JP 61308989A JP 30898986 A JP30898986 A JP 30898986A JP S63240941 A JPS63240941 A JP S63240941A
Authority
JP
Japan
Prior art keywords
oxidizing gas
reactor
primary
zone
raw material
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.)
Granted
Application number
JP61308989A
Other languages
English (en)
Japanese (ja)
Other versions
JPH0525538B2 (enExample
Inventor
ジャック アレジイ
クリスタイン ブソン
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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 IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of JPS63240941A publication Critical patent/JPS63240941A/ja
Publication of JPH0525538B2 publication Critical patent/JPH0525538B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J12/00Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/005Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor carried out at high temperatures, e.g. by pyrolysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24Stationary reactors without moving elements inside
    • B01J19/2415Tubular reactors
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/04Feed or outlet devices; Feed or outlet control devices using osmotic pressure using membranes, porous plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00085Plates; Jackets; Cylinders
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/0015Controlling the temperature by thermal insulation means
    • B01J2219/00155Controlling the temperature by thermal insulation means using insulating materials or refractories
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00159Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02Apparatus characterised by their chemically-resistant properties
    • B01J2219/025Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0263Ceramic

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
JP61308989A 1985-12-30 1986-12-26 気相下の被酸化性原料の酸化方法とこの方法を実施する反応器 Granted JPS63240941A (ja)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8519431A FR2592320B1 (fr) 1985-12-30 1985-12-30 Nouveau procede d'oxydation d'une charge oxydable en phase gazeuse et reacteur pour la mise en oeuvre de ce procede.
FR85/19431 1985-12-30

Publications (2)

Publication Number Publication Date
JPS63240941A true JPS63240941A (ja) 1988-10-06
JPH0525538B2 JPH0525538B2 (enExample) 1993-04-13

Family

ID=9326318

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61308989A Granted JPS63240941A (ja) 1985-12-30 1986-12-26 気相下の被酸化性原料の酸化方法とこの方法を実施する反応器

Country Status (11)

Country Link
US (1) US5037619A (enExample)
EP (1) EP0231706B1 (enExample)
JP (1) JPS63240941A (enExample)
BR (1) BR8606526A (enExample)
CA (1) CA1297677C (enExample)
DE (1) DE3662177D1 (enExample)
DK (1) DK168365B1 (enExample)
FR (1) FR2592320B1 (enExample)
MY (1) MY101130A (enExample)
NO (1) NO166844C (enExample)
NZ (1) NZ218796A (enExample)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01281139A (ja) * 1988-03-16 1989-11-13 Inst Fr Petrole 気相において酸化しうる仕込原料の酸化方法およびこの方法の実施のための反応器
JP2004002184A (ja) * 2002-05-02 2004-01-08 Daimler Chrysler Ag 反応室に流入する混合気のフラッシュバックを防止する方法
JP2007513762A (ja) * 2003-12-09 2007-05-31 ポコ・グラフアイト・インコーポレーテツド 好ましくないガス混合無しで、高温用加工体を通る二種のガス送出用のシステム、方法及び装置
JP2009536143A (ja) * 2006-05-08 2009-10-08 コンパクトジーティーエル パブリック リミテッド カンパニー 交互に配置された第一および第二フローチャネルを備えた触媒作用反応器

Families Citing this family (38)

* Cited by examiner, † Cited by third party
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DZ1444A1 (fr) * 1989-09-12 2004-09-13 Inst Francais Du Petrole Procédé et réacteur d'oxydation à differentiel de perte de charge et son utilisation.
FR2651689B1 (fr) * 1989-09-12 1991-10-31 Inst Francais Du Petrole Reacteur d'oxydation a differentiel de perte de charge et son utilisation.
JP3096302B2 (ja) * 1989-12-11 2000-10-10 ゲブリユーダー ズルツアー アクチエンゲゼルシヤフト 不均一反応型の反応器及び反応器用触媒
US5254318A (en) * 1992-07-20 1993-10-19 Stone & Webster Engineering Corporation Lined reformer tubes for high pressure reformer reactors
CN1125933A (zh) * 1994-02-15 1996-07-03 日本工机株式会社 气体发生剂组合物、其制剂化方法和运输方法
US5518700A (en) * 1994-06-25 1996-05-21 Shell Oil Company Cyclonic reactor
US5595712A (en) * 1994-07-25 1997-01-21 E. I. Du Pont De Nemours And Company Chemical mixing and reaction apparatus
US5980596A (en) * 1997-04-25 1999-11-09 Exxon Research And Engineering Co. Multi-injector autothermal reforming process and apparatus for producing synthesis gas (law 565).
US6267912B1 (en) * 1997-04-25 2001-07-31 Exxon Research And Engineering Co. Distributed injection catalytic partial oxidation process and apparatus for producing synthesis gas
US5883138A (en) * 1997-04-25 1999-03-16 Exxon Research And Engineering Company Rapid injection catalytic partial oxidation process and apparatus for producing synthesis gas (law 562)
US6168765B1 (en) * 1998-09-08 2001-01-02 Uop Llc Process and apparatus for interbed injection in plate reactor arrangement
US6481200B1 (en) * 1999-10-22 2002-11-19 Toyota Jidosha Kabushiki Kaisha Catalyst warming apparatus of internal combustion engine
DE10042746A1 (de) * 2000-08-31 2002-03-28 Degussa Verfahren und Vorrichtung zum Durchführen von Reaktionen in einem Reaktor mit spaltförmigen Reaktionsräumen
CA2357527C (en) 2001-10-01 2009-12-01 Technology Convergence Inc. Methanol recycle stream
US20040171701A1 (en) * 2001-11-02 2004-09-02 Technology Convergence Inc. Methanol production process
US20030086845A1 (en) * 2001-11-05 2003-05-08 Adusei George Y. Catalytic reactor
RU2181622C1 (ru) * 2001-11-29 2002-04-27 Закрытое акционерное общество "Метанол" Установка для гомогенного окисления природного газа и способ гомогенного окисления природного газа
US20030173205A1 (en) * 2002-03-12 2003-09-18 Arne Karlsson Process vessel with integral evaporator
US6936366B2 (en) 2002-04-03 2005-08-30 Hewlett-Packard Development Company, L.P. Single chamber solid oxide fuel cell architecture for high temperature operation
ES2217928B1 (es) * 2002-06-10 2006-03-16 Universidad De Cordoba Reactor modular acoplable a plasmas de alta frecuencia de libre expansion.
US20040120871A1 (en) * 2002-12-19 2004-06-24 Gilbert De Angelis Reactor construction
FR2850372B1 (fr) * 2003-01-23 2006-06-09 Inst Francais Du Petrole Nouveau reacteur d'oxydation partielle
US20040173597A1 (en) * 2003-03-03 2004-09-09 Manoj Agrawal Apparatus for contacting gases at high temperature
US7108838B2 (en) * 2003-10-30 2006-09-19 Conocophillips Company Feed mixer for a partial oxidation reactor
US7465326B2 (en) * 2003-12-09 2008-12-16 Panasonic Corporation Hydrogen generating apparatus
FR2879594B1 (fr) * 2004-12-17 2007-02-02 Air Liquide Ensemble de jonction ceramique-metal ou alliage metallique
GB0508096D0 (en) * 2005-04-21 2005-06-01 Knitmesh Ltd Detonation flame arrestor
US8403557B2 (en) * 2006-09-28 2013-03-26 University Of Washington Micromixer using integrated three-dimensional porous structure
JP2010505393A (ja) * 2006-09-28 2010-02-25 ユニヴァーシティ オブ ワシントン 3dマイクロスケールの人工組織モデルシステム
US8247464B2 (en) 2006-09-28 2012-08-21 University Of Washington Method of selective foaming for porous polymeric material
JP5435846B2 (ja) 2007-07-30 2014-03-05 日揮株式会社 ガス混合装置及び合成ガス製造装置
EP2249951B1 (en) * 2007-12-14 2014-01-01 Dow Technology Investments LLC Low shear gas mixer
WO2009078899A1 (en) * 2007-12-14 2009-06-25 Dow Technology Investments Llc Oxygen/hydrocarbon rapid (high shear) gas mixer, particularly for the production of ethylene oxide
BRPI0816635B1 (pt) * 2007-12-14 2016-07-26 Dow Technology Investments Llc sistema para a produção de óxido de etileno, método para misturar um gás contendo oxigênio com um gás contendo hidrocarboneto e sistema de oxidação parcial
US8334395B2 (en) * 2007-12-14 2012-12-18 Dow Technology Investments Llc Hydrocarbon/oxygen industrial gas mixer with coarse water droplet environment to reduce ignition potential
CA2701590C (en) * 2007-12-14 2016-06-28 Dow Technology Investments Llc Hydrocarbon/oxygen industrial gas mixer with water mist
MX2016002939A (es) * 2013-09-09 2016-07-26 Zoneflow Reactor Technologies Llc Reactor catalitico no adiabatico.
EP3206017B1 (de) * 2016-02-09 2018-09-12 Elster GmbH Sensor und verfahren zur bestimmung der luftzahl eines brenngas-luft-gemisches

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2621117A (en) * 1947-03-11 1952-12-09 Texaco Development Corp Preparation of hydrogen and carbon monoxide gas mixtures
US3706534A (en) * 1970-11-03 1972-12-19 Shell Oil Co Mixing nozzle for gases
US3741533A (en) * 1971-10-14 1973-06-26 Dow Chemical Co Mixing apparatus
US4222671A (en) * 1978-09-05 1980-09-16 Gilmore Oscar Patrick Static mixer
EP0025308B1 (en) * 1979-09-06 1984-07-11 Imperial Chemical Industries Plc A process and apparatus for catalytically reacting steam with a hydrocarbon in endothermic conditions
US4378336A (en) * 1979-12-18 1983-03-29 Conoco Inc. Monolith reactor
US4381187A (en) * 1980-03-24 1983-04-26 United Technologies Corporation Process for gasifying liquid hydrocarbon fuels
JPS59186621A (ja) * 1983-04-05 1984-10-23 Ngk Insulators Ltd 多孔体
US4614440A (en) * 1985-03-21 1986-09-30 Komax Systems, Inc. Stacked motionless mixer

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01281139A (ja) * 1988-03-16 1989-11-13 Inst Fr Petrole 気相において酸化しうる仕込原料の酸化方法およびこの方法の実施のための反応器
JP2004002184A (ja) * 2002-05-02 2004-01-08 Daimler Chrysler Ag 反応室に流入する混合気のフラッシュバックを防止する方法
JP2007513762A (ja) * 2003-12-09 2007-05-31 ポコ・グラフアイト・インコーポレーテツド 好ましくないガス混合無しで、高温用加工体を通る二種のガス送出用のシステム、方法及び装置
JP2009536143A (ja) * 2006-05-08 2009-10-08 コンパクトジーティーエル パブリック リミテッド カンパニー 交互に配置された第一および第二フローチャネルを備えた触媒作用反応器

Also Published As

Publication number Publication date
BR8606526A (pt) 1987-10-20
DK168365B1 (da) 1994-03-21
CA1297677C (fr) 1992-03-24
NO166844C (no) 1991-09-11
FR2592320A1 (fr) 1987-07-03
US5037619A (en) 1991-08-06
NO865278D0 (no) 1986-12-23
NO865278L (no) 1987-07-01
NZ218796A (en) 1989-01-06
DK627586D0 (da) 1986-12-23
MY101130A (en) 1991-07-31
NO166844B (no) 1991-06-03
EP0231706A1 (fr) 1987-08-12
EP0231706B1 (fr) 1989-03-01
DE3662177D1 (en) 1989-04-06
DK627586A (da) 1987-07-01
FR2592320B1 (fr) 1988-04-08
JPH0525538B2 (enExample) 1993-04-13

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