GB916981A - Improvements in or relating to steam reforming hydrocarbons - Google Patents

Improvements in or relating to steam reforming hydrocarbons

Info

Publication number
GB916981A
GB916981A GB801259A GB801259A GB916981A GB 916981 A GB916981 A GB 916981A GB 801259 A GB801259 A GB 801259A GB 801259 A GB801259 A GB 801259A GB 916981 A GB916981 A GB 916981A
Authority
GB
United Kingdom
Prior art keywords
steam reforming
relating
mixture
reforming hydrocarbons
catalyst
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.)
Expired
Application number
GB801259A
Inventor
John George Mackay Bremner
Thomas James Perrett Pearce
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.)
Imperial Chemical Industries Ltd
Original Assignee
Imperial Chemical Industries 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 Imperial Chemical Industries Ltd filed Critical Imperial Chemical Industries Ltd
Priority to GB801259A priority Critical patent/GB916981A/en
Publication of GB916981A publication Critical patent/GB916981A/en
Expired 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
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Catalysts (AREA)

Abstract

Hydrogen and oxides of carbon are obtained by a steam reforming process in which a normally liquid hydrocarbon is admixed with the quantity of water required to give a mixture of a specified composition, emulsifying the mixture and then passing it continuously to a vaporization zone and then over a steam reforming catalyst. In an example, a petroleum fraction of boiling range 30 DEG -180 DEG C. is intimately mixed with 7 times its weight of water, emulsified and pumped to a mono-tube boiler and pre-heated to 400 DEG C., and then passed over a catalyst which may be nickel.
GB801259A 1959-03-09 1959-03-09 Improvements in or relating to steam reforming hydrocarbons Expired GB916981A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB801259A GB916981A (en) 1959-03-09 1959-03-09 Improvements in or relating to steam reforming hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB801259A GB916981A (en) 1959-03-09 1959-03-09 Improvements in or relating to steam reforming hydrocarbons

Publications (1)

Publication Number Publication Date
GB916981A true GB916981A (en) 1963-01-30

Family

ID=9844092

Family Applications (1)

Application Number Title Priority Date Filing Date
GB801259A Expired GB916981A (en) 1959-03-09 1959-03-09 Improvements in or relating to steam reforming hydrocarbons

Country Status (1)

Country Link
GB (1) GB916981A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0205146A2 (en) * 1985-06-11 1986-12-17 Energy Research Corporation Fuel cell system with premixing of water miscible hydrocarbon fuel and water
WO2003040030A1 (en) * 2001-11-05 2003-05-15 The Lubrizol Corporation Process for making hydrogen gas

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0205146A2 (en) * 1985-06-11 1986-12-17 Energy Research Corporation Fuel cell system with premixing of water miscible hydrocarbon fuel and water
EP0205146A3 (en) * 1985-06-11 1987-08-05 Energy Research Corporation Fuel cell system with premixing of water miscible hydrocarbon fuel and water
WO2003040030A1 (en) * 2001-11-05 2003-05-15 The Lubrizol Corporation Process for making hydrogen gas

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