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AU1029001A - Autothermic reactor circuit for direct coupling of endothermic and exothermic reactions - Google Patents

Autothermic reactor circuit for direct coupling of endothermic and exothermic reactions

Info

Publication number
AU1029001A
AU1029001A AU10290/01A AU1029001A AU1029001A AU 1029001 A AU1029001 A AU 1029001A AU 10290/01 A AU10290/01 A AU 10290/01A AU 1029001 A AU1029001 A AU 1029001A AU 1029001 A AU1029001 A AU 1029001A
Authority
AU
Australia
Prior art keywords
endothermic
direct coupling
exothermic reactions
reactor circuit
autothermic 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.)
Abandoned
Application number
AU10290/01A
Inventor
Gerhart Eigenberger
Jorg Frauhammer
Grigorios Kolios
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.)
Universitaet Stuttgart
Original Assignee
Universitaet Stuttgart
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 Universitaet Stuttgart filed Critical Universitaet Stuttgart
Publication of AU1029001A publication Critical patent/AU1029001A/en
Abandoned legal-status Critical Current

Links

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
    • C01B3/38—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 catalysts
    • C01B3/384—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 catalysts the catalyst being continuously externally heated
    • 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
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/2485—Monolithic 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/24—Stationary reactors without moving elements inside
    • B01J19/248—Reactors comprising multiple separated flow channels
    • B01J19/249—Plate-type 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0207—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal
    • B01J8/0235—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid flow within the bed being predominantly horizontal in a spiral shaped bed
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285—Heating or cooling the reactor
    • 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
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • 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
    • C01B3/38—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 catalysts
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00309—Controlling the temperature by indirect heat exchange with two or more reactions in heat exchange with each other, such as an endothermic reaction in heat exchange with an exothermic reaction
    • 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
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2451—Geometry of the reactor
    • B01J2219/2453—Plates arranged in parallel
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2462—Heat exchange aspects the reactants being in indirect heat exchange with a non reacting heat exchange medium
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2461—Heat exchange aspects
    • B01J2219/2465—Two reactions in indirect heat exchange with each other
    • 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2474—Mixing means, e.g. fins or baffles attached to the 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
    • B01J2219/24—Stationary reactors without moving elements inside
    • B01J2219/2401—Reactors comprising multiple separate flow channels
    • B01J2219/245—Plate-type reactors
    • B01J2219/2476—Construction materials
    • B01J2219/2477—Construction materials of the catalysts
    • 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
    • Y02P20/10—Process efficiency

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Fluid Mechanics (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
AU10290/01A 1999-11-04 2000-11-06 Autothermic reactor circuit for direct coupling of endothermic and exothermic reactions Abandoned AU1029001A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19953233A DE19953233A1 (en) 1999-11-04 1999-11-04 Autothermal reactor circuits for the direct coupling of endothermic and exothermic reactions
DE19953233 1999-11-04
PCT/EP2000/010928 WO2001032302A1 (en) 1999-11-04 2000-11-06 Autothermic reactor circuit for direct coupling of endothermic and exothermic reactions

Publications (1)

Publication Number Publication Date
AU1029001A true AU1029001A (en) 2001-05-14

Family

ID=7927994

Family Applications (1)

Application Number Title Priority Date Filing Date
AU10290/01A Abandoned AU1029001A (en) 1999-11-04 2000-11-06 Autothermic reactor circuit for direct coupling of endothermic and exothermic reactions

Country Status (4)

Country Link
EP (1) EP1230006A1 (en)
AU (1) AU1029001A (en)
DE (1) DE19953233A1 (en)
WO (1) WO2001032302A1 (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10239547A1 (en) * 2002-08-23 2004-03-04 Eigenberger, Gerhart, Prof.Dr.-Ing. Process for autothermally carrying out endothermic high temperature reactions comprises continuously introducing a reaction mixture having a low temperature to the front end of the reactor during the production phase, and further processing
US6936238B2 (en) * 2002-09-06 2005-08-30 General Motors Corporation Compact partial oxidation/steam reactor with integrated air preheater, fuel and water vaporizer
DE10352798A1 (en) * 2003-11-12 2005-06-23 Robert Bosch Gmbh Fuel reformer for the production of hydrogen, in particular for the operation of a fuel cell
DE10359205B4 (en) * 2003-12-17 2007-09-06 Webasto Ag Reformer and method for converting fuel and oxidant to reformate
DE102004007344A1 (en) * 2004-02-14 2005-09-01 Robert Bosch Gmbh Integrated reactor for the thermal coupling of reactions and methods for controlling the temperature field in such a reactor
DE102006033441B4 (en) * 2006-06-29 2009-05-07 Enerday Gmbh Reformer for a fuel cell system
DE102006040563A1 (en) * 2006-08-30 2008-03-20 Enerday Gmbh Method and system for adjusting the temperature profile of a catalyst in a reformer
DE102007040037A1 (en) 2007-08-24 2009-02-26 Modine Manufacturing Co., Racine Plant for soldering and process
PL2262734T3 (en) 2008-03-31 2012-03-30 Basf Se Improved method for producing hydrogen cyanide through catalytic dehydration of gaseous formamide direct heating
CN103299301B (en) 2011-06-17 2015-07-01 乐天株式会社 Information processing device, information processing method, information processing program, and recording medium recording information processing program
DE102016204840A1 (en) * 2016-03-23 2017-09-28 Thyssenkrupp Ag Temperature-optimized device for reactions of gaseous media and method for the thermal homogenization of a reaction region
ES2939236T3 (en) 2020-06-30 2023-04-20 Aura Tech Gmbh Procedure and device for recycling waste materials containing valuable metals

Family Cites Families (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2655442A (en) * 1948-08-23 1953-10-13 Phillips Petroleum Co Process and apparatus for the manufacture of synthesis gas
NL6611310A (en) * 1965-08-18 1967-02-20
DE3042142C2 (en) * 1980-11-03 1983-06-23 Mannesmann AG, 4000 Düsseldorf Fluidized bed gas generator
DE3402713A1 (en) * 1984-01-26 1985-08-08 Linde Ag, 6200 Wiesbaden METHOD AND REACTOR FOR CARRYING OUT AN ENDOTHERMAL REACTION
DE3439174A1 (en) * 1984-10-25 1986-05-07 Linde Ag, 6200 Wiesbaden METHOD AND REACTOR FOR CARRYING OUT AN ENDOTHERMAL REACTION
DK165946C (en) * 1985-03-21 1993-07-05 Haldor Topsoe As REFORMING PROCESS DURING HEAT EXCHANGE AND REACTOR THEREOF
US4909808A (en) * 1987-10-14 1990-03-20 The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration Steam reformer with catalytic combustor
JPH01261201A (en) * 1988-04-12 1989-10-18 Mitsubishi Gas Chem Co Inc Hydrocarbon reforming reactor
DE3813863A1 (en) * 1988-04-23 1989-11-02 Uhde Gmbh DEVICE FOR RECEIVING CATALYSTS, ESPECIALLY IN THE PRODUCTION OF SYNTHESIS GAS
GB2217728B (en) * 1988-04-28 1992-02-26 Humphreys & Glasgow Ltd Combined reformer
JPH0218303A (en) * 1988-07-07 1990-01-22 Mitsubishi Gas Chem Co Inc Reactor and process for reforming hydrocarbon
CA2054260A1 (en) * 1990-11-01 1992-05-02 Gregory D. Snyder Combined prereformer and convetive heat transfer reformer
US5270127A (en) * 1991-08-09 1993-12-14 Ishikawajima-Harima Heavy Industries Co., Ltd. Plate shift converter
GB9225188D0 (en) * 1992-12-02 1993-01-20 Rolls Royce & Ass Combined reformer and shift reactor
CN1094465C (en) * 1996-06-28 2002-11-20 松下电工株式会社 Modification apparatus
DE19647527C1 (en) * 1996-11-16 1998-03-12 Degussa Cyano compounds preparation
DE19727841A1 (en) * 1997-06-24 1999-01-07 Fraunhofer Ges Forschung Method and device for the autothermal reforming of hydrocarbons
DE19832386A1 (en) * 1998-07-18 2000-01-27 Dbb Fuel Cell Engines Gmbh Reforming reactor with catalytic burner unit

Also Published As

Publication number Publication date
DE19953233A1 (en) 2001-05-10
WO2001032302A1 (en) 2001-05-10
EP1230006A1 (en) 2002-08-14

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Legal Events

Date Code Title Description
MK6 Application lapsed section 142(2)(f)/reg. 8.3(3) - pct applic. not entering national phase