GB1290231A - - Google Patents

Info

Publication number
GB1290231A
GB1290231A GB1290231DA GB1290231A GB 1290231 A GB1290231 A GB 1290231A GB 1290231D A GB1290231D A GB 1290231DA GB 1290231 A GB1290231 A GB 1290231A
Authority
GB
United Kingdom
Prior art keywords
gas
refinery
range
reformer
producer
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
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 filed Critical
Publication of GB1290231A publication Critical patent/GB1290231A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/20—Purifying combustible gases containing carbon monoxide by treating with solids; Regenerating spent purifying masses
    • C10K1/30—Purifying combustible gases containing carbon monoxide by treating with solids; Regenerating spent purifying masses with moving purifying masses
    • 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

Landscapes

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

Abstract

1290231 Combustible gas HYDROCARBON RESEARCH Inc 5 May 1970 [29 May 1969] 21685/70 Heading C5E Natural gas, refinery gas or naphtha is steam reformed in catalyst-filled tubes 46 in a reformer 30 heated by combusting producer gas which has been purified at 20 by contact with a particulate metal oxide comprising one or more of the oxides of Fe, Mn, Ni and Ca at a temperature in the range 800‹ to 1400‹ F. Reformer temperatures lie in the range 800‹ to 1700‹ F. and the oxide is regenerated with air, e.g. in a fluidized bed 32, solids, fly ash, and tars having been separated at 22, 24 from the producer gas. The method is applicable to a refinery where coal is catalytically hydrogenated to make gasoline, the required hydrogen being obtained from the refinery gas by the above method.
GB1290231D 1969-05-29 1970-05-05 Expired GB1290231A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US82883069A 1969-05-29 1969-05-29

Publications (1)

Publication Number Publication Date
GB1290231A true GB1290231A (en) 1972-09-20

Family

ID=25252850

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1290231D Expired GB1290231A (en) 1969-05-29 1970-05-05

Country Status (4)

Country Link
DE (2) DE2026389A1 (en)
FR (1) FR2048971A5 (en)
GB (1) GB1290231A (en)
ZA (1) ZA703441B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4710483A (en) * 1977-07-21 1987-12-01 Trw Inc. Novel carbonaceous material and process for producing a high BTU gas from this material
FR2443643A1 (en) * 1978-12-06 1980-07-04 Creusot Loire HEATING APPARATUS PROVIDING WATER VAPOR AND HOT GAS

Also Published As

Publication number Publication date
ZA703441B (en) 1971-02-24
DE2026389A1 (en) 1971-06-16
FR2048971A5 (en) 1971-03-19
DE2060589A1 (en) 1972-01-13

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Legal Events

Date Code Title Description
PS Patent sealed
PLNP Patent lapsed through nonpayment of renewal fees