GB631319A - An improved production of gaseous and liquid fuels from carbonaceous materials - Google Patents

An improved production of gaseous and liquid fuels from carbonaceous materials

Info

Publication number
GB631319A
GB631319A GB2332746A GB2332746A GB631319A GB 631319 A GB631319 A GB 631319A GB 2332746 A GB2332746 A GB 2332746A GB 2332746 A GB2332746 A GB 2332746A GB 631319 A GB631319 A GB 631319A
Authority
GB
United Kingdom
Prior art keywords
fuel
liquid
gas
gaseous
tail 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.)
Expired
Application number
GB2332746A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
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 Standard Oil Development Co filed Critical Standard Oil Development Co
Priority to GB2332746A priority Critical patent/GB631319A/en
Publication of GB631319A publication Critical patent/GB631319A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/22Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/36Production 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 oxygen or mixtures containing oxygen as gasifying agents

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

A process wherein solid carbonaceous materials are converted into liquid and gaseous fuels and in which the relative production of either fuel is co-ordinated to the seasonal demand for fuel gas and motor fuel, comprises subjecting the carbonaceous material to a treatment comprising a gasification reaction with steam to produce gases containing CO and H2 which are converted by a catalytic treatment into normally liquid hydrocarbons and a tail gas, liquid hydrocarbons are recovered and some of the tail gas is treated, e.g. by washing to remove CO2 to render the gas suitable for use as a fuel gas and a portion determined by the demand for fuel gas is re-cycled to the gasification step where it may be used as a source of heat for the process or be passed through the generator either to crack the residual hydrocarbons in the tail gas to form additional quantities of CO and H2 or to pass through the fuel bed substantially unchanged and to modify the composition of the gases containing CO and H2. The choice and age of the catalyst and the conditions under which the synthesis is carried out affords an additional means of controlling the liquid-gaseous fuel production. The usual synthesis catalysts, e.g. iron or cobalt, may be used at temperatures ranging from 350-800 DEG F. and pressures ranging from 1-50 atmospheres. The liquid synthetic products may be refined by any conventional method.
GB2332746A 1946-08-06 1946-08-06 An improved production of gaseous and liquid fuels from carbonaceous materials Expired GB631319A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2332746A GB631319A (en) 1946-08-06 1946-08-06 An improved production of gaseous and liquid fuels from carbonaceous materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2332746A GB631319A (en) 1946-08-06 1946-08-06 An improved production of gaseous and liquid fuels from carbonaceous materials

Publications (1)

Publication Number Publication Date
GB631319A true GB631319A (en) 1949-11-01

Family

ID=10193816

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2332746A Expired GB631319A (en) 1946-08-06 1946-08-06 An improved production of gaseous and liquid fuels from carbonaceous materials

Country Status (1)

Country Link
GB (1) GB631319A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2702238A (en) * 1950-11-20 1955-02-15 Phillips Petroleum Co Apparatus for controlling synthesis reactions
FR2190722A1 (en) * 1972-06-28 1974-02-01 Texaco Development Corp

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2702238A (en) * 1950-11-20 1955-02-15 Phillips Petroleum Co Apparatus for controlling synthesis reactions
FR2190722A1 (en) * 1972-06-28 1974-02-01 Texaco Development Corp

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