JPS6428201A - Methanol modification equipment - Google Patents

Methanol modification equipment

Info

Publication number
JPS6428201A
JPS6428201A JP62184533A JP18453387A JPS6428201A JP S6428201 A JPS6428201 A JP S6428201A JP 62184533 A JP62184533 A JP 62184533A JP 18453387 A JP18453387 A JP 18453387A JP S6428201 A JPS6428201 A JP S6428201A
Authority
JP
Japan
Prior art keywords
tube
reaction zone
reaction
modification
gas
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.)
Pending
Application number
JP62184533A
Other languages
Japanese (ja)
Inventor
Toshihiro Sugiyama
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP62184533A priority Critical patent/JPS6428201A/en
Publication of JPS6428201A publication Critical patent/JPS6428201A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • H01M8/0625Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material in a modular combined reactor/fuel cell structure
    • H01M8/0631Reactor construction specially adapted for combination reactor/fuel cell
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Fuel Cell (AREA)

Abstract

PURPOSE:To reduce the carbon monoxide concentration in the modified gas produced and to prevent the modification catalyst from deterioration, by connecting, in a continuous manner, between the cylindrical outer reaction zone formed by the inner and outer tubes and the inner reaction zone in the inner tube in a reaction tube as a duplex tube structure. CONSTITUTION:The reaction tube 17 in a methanol modification equipment 30, which is made up of, as a duplex tube structure, a inner tube 18 and outer tube 19, is packed with a modification catalyst 16. The cylindrical outer reaction zone 20 formed by said inner tube 18 and outer tube 19 is closed with the upper plate 22 on the modified gas outlet chamber 21 at the bottom of the oven 5. The inner reaction zone 23 in the inner tube 18 and the outer reaction zone 20 are connected at the upper part of the reaction tube 17 to form a continuous reaction space. Methanol stock gas overheated by a vaporizer 13 is fed via a manifold 23 to the outer reaction zone 20, rising followed by turning back at the upper part of the reaction tube 17, then flowing down through the inner reaction zone 23 and flowing into the modification gas outlet chamber 21. During the above process, the stock gas is modified into hydrogen-rich gas by the action of the modification catalyst 16.
JP62184533A 1987-07-23 1987-07-23 Methanol modification equipment Pending JPS6428201A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62184533A JPS6428201A (en) 1987-07-23 1987-07-23 Methanol modification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62184533A JPS6428201A (en) 1987-07-23 1987-07-23 Methanol modification equipment

Publications (1)

Publication Number Publication Date
JPS6428201A true JPS6428201A (en) 1989-01-30

Family

ID=16154864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62184533A Pending JPS6428201A (en) 1987-07-23 1987-07-23 Methanol modification equipment

Country Status (1)

Country Link
JP (1) JPS6428201A (en)

Similar Documents

Publication Publication Date Title
JPS644232A (en) Endothermic reaction apparatus for gases
CA2190893A1 (en) Process for Producing Syngas and Hydrogen from Natural Gas Using a Membrane Reactor
UA8348A1 (en) converter for ammonia synthesis
MY101681A (en) Autothermal production of synthesis gas.
FR2469446A1 (en) PROCESS FOR THE RAPID PRODUCTION OF OLEFINS BY THERMAL CONVERSION OF HYDROCARBONS IN THE PRESENCE OF HYDROGEN
CA2038289A1 (en) Endothermic reaction apparatus
FR2456708A1 (en) HYDROCARBON REFORMING PROCESS AND APPARATUS FOR IMPLEMENTING SAME
Gesser et al. The CO 2 reforming of natural gas in a silent discharge reactor
NO163732C (en) DEVICE FOR PRODUCING GAS WITH HYDROGEN AND CARBONOX ACID CONTENT.
ATE66900T1 (en) INTERNAL HEAT RECOVERY STEAM REFORMER.
DE3564417D1 (en) Process and device for the reforming of methanol
GB1470631A (en) Tubular heater for catalytically cracking hydrocarbons
JPS6428201A (en) Methanol modification equipment
EP0235367A3 (en) Apparatus to be used in a process for the production of a synthesis gaz containing hydrogen and carbon monoxide
ES8106865A1 (en) Apparatus for the production of ammonia synthesis gas from purified coke oven gas
JPS57192489A (en) Hydrocarbon reforming furnace
NO951103L (en) Process for producing synthesis gas
JPS51122102A (en) Process for producing fuel gas using methanol as the starting raw mate rial
JPS6442301A (en) Production of hydrogen
GB684127A (en) Improvements in or relating to apparatus for conducting a contact process
JPS55155088A (en) Tubular reactor for coal liquefaction
EP0298772B1 (en) Chemical reactor
JPS6428202A (en) Methanol modification equipment
GB2003914A (en) Multiple-stage hydrocarbon conversion with gravity-flowing catalyst particles
JPS646092A (en) Production of methane-containing fuel gas from methanol