DK168365B1 - Fremgangsmåde til oxidation af en oxiderbar charge i gasfase med en gasblanding og reaktor til udøvelse af fremgangsmåden - Google Patents

Fremgangsmåde til oxidation af en oxiderbar charge i gasfase med en gasblanding og reaktor til udøvelse af fremgangsmåden Download PDF

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Publication number
DK168365B1
DK168365B1 DK627586A DK627586A DK168365B1 DK 168365 B1 DK168365 B1 DK 168365B1 DK 627586 A DK627586 A DK 627586A DK 627586 A DK627586 A DK 627586A DK 168365 B1 DK168365 B1 DK 168365B1
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DK
Denmark
Prior art keywords
gas
zone
distribution
mixing
filling
Prior art date
Application number
DK627586A
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Danish (da)
English (en)
Other versions
DK627586A (da
DK627586D0 (da
Inventor
Jacques Alagy
Christian Busson
Original Assignee
Inst Francais Du Petrole
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 Inst Francais Du Petrole filed Critical Inst Francais Du Petrole
Publication of DK627586D0 publication Critical patent/DK627586D0/da
Publication of DK627586A publication Critical patent/DK627586A/da
Application granted granted Critical
Publication of DK168365B1 publication Critical patent/DK168365B1/da

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Classifications

    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J12/00—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor
    • B01J12/005—Chemical processes in general for reacting gaseous media with gaseous media; Apparatus specially adapted therefor carried out at high temperatures, e.g. by pyrolysis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/2415—Tubular reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/04—Feed or outlet devices; Feed or outlet control devices using osmotic pressure using membranes, porous plates
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
    • B01J2219/00085—Plates; Jackets; Cylinders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/0015—Controlling the temperature by thermal insulation means
    • B01J2219/00155—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00159—Controlling the temperature controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02—Apparatus characterised by their chemically-resistant properties
    • B01J2219/025—Apparatus characterised by their chemically-resistant properties characterised by the construction materials of the reactor vessel proper
    • B01J2219/0263—Ceramic

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
DK627586A 1985-12-30 1986-12-23 Fremgangsmåde til oxidation af en oxiderbar charge i gasfase med en gasblanding og reaktor til udøvelse af fremgangsmåden DK168365B1 (da)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8519431 1985-12-30
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.

Publications (3)

Publication Number Publication Date
DK627586D0 DK627586D0 (da) 1986-12-23
DK627586A DK627586A (da) 1987-07-01
DK168365B1 true DK168365B1 (da) 1994-03-21

Family

ID=9326318

Family Applications (1)

Application Number Title Priority Date Filing Date
DK627586A DK168365B1 (da) 1985-12-30 1986-12-23 Fremgangsmåde til oxidation af en oxiderbar charge i gasfase med en gasblanding og reaktor til udøvelse af fremgangsmåden

Country Status (11)

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

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FR2628727B1 (fr) * 1988-03-16 1990-08-24 Inst Francais Du Petrole Procede d'oxydation d'une charge oxydable en phase gazeuse et reacteur pour la mise en oeuvre de ce procede
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
WO1995021805A1 (fr) * 1994-02-15 1995-08-17 Nippon Koki Co., Ltd. Composition gazogene, procede de fabrication de comprimes de ladite composition et procede de transport associe
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
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)
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
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
DE10219747B4 (de) * 2002-05-02 2005-06-23 Daimlerchrysler Ag Verfahren zur Vermeidung einer Rückzündung in einem einen Reaktionsraum anströmenden Gemisch und Reaktor zur Durchführung des Verfahrens
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
US7258137B2 (en) * 2003-12-09 2007-08-21 Poco Graphite, Inc. System, method, and apparatus for dual gas delivery through a high temperature artifact without undesirable gas mixing
WO2005056468A1 (ja) * 2003-12-09 2005-06-23 Matsushita Electric Industrial Co., Ltd. 水素生成装置
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
GB0608927D0 (en) * 2006-05-08 2006-06-14 Accentus Plc Catalytic Reactor
US8247464B2 (en) 2006-09-28 2012-08-21 University Of Washington Method of selective foaming for porous polymeric material
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
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
WO2009078898A1 (en) * 2007-12-14 2009-06-25 Dow Technology Investments Llc Hydrocarbon/oxygen industrial gas mixer with coarse water droplet environment to reduce ignition potential
US8500320B2 (en) * 2007-12-14 2013-08-06 Dow Technology Investments Llc Low shear gas mixer
EP2229372B1 (en) * 2007-12-14 2013-04-10 Dow Technology Investments LLC Wet scrubbing for removing particulate solids from oxygen supply line
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
CN101848760B (zh) * 2007-12-14 2014-04-02 陶氏技术投资有限公司 使用水雾的烃/氧工业气体混合器
JP2016531750A (ja) * 2013-09-09 2016-10-13 ゾーンフロー リアクター テクノロジーズ エルエルシー 非断熱触媒反応器
EP3206017B1 (de) * 2016-02-09 2018-09-12 Elster GmbH Sensor und verfahren zur bestimmung der luftzahl eines brenngas-luft-gemisches

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Also Published As

Publication number Publication date
NZ218796A (en) 1989-01-06
NO865278L (no) 1987-07-01
DK627586A (da) 1987-07-01
US5037619A (en) 1991-08-06
NO166844C (no) 1991-09-11
CA1297677C (fr) 1992-03-24
EP0231706A1 (fr) 1987-08-12
NO865278D0 (no) 1986-12-23
BR8606526A (pt) 1987-10-20
MY101130A (en) 1991-07-31
JPS63240941A (ja) 1988-10-06
DE3662177D1 (en) 1989-04-06
DK627586D0 (da) 1986-12-23
FR2592320B1 (fr) 1988-04-08
FR2592320A1 (fr) 1987-07-03
JPH0525538B2 (ja) 1993-04-13
EP0231706B1 (fr) 1989-03-01
NO166844B (no) 1991-06-03

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