GB1111643A - Making methane-rich gas - Google Patents

Making methane-rich gas

Info

Publication number
GB1111643A
GB1111643A GB5016563A GB5016563A GB1111643A GB 1111643 A GB1111643 A GB 1111643A GB 5016563 A GB5016563 A GB 5016563A GB 5016563 A GB5016563 A GB 5016563A GB 1111643 A GB1111643 A GB 1111643A
Authority
GB
United Kingdom
Prior art keywords
nickel
hydrogen
catalyst
chromite
methane
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
GB5016563A
Inventor
David Owen Hughes
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 GB5016563A priority Critical patent/GB1111643A/en
Publication of GB1111643A publication Critical patent/GB1111643A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G47/00Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
    • C10G47/02Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
    • C10G47/10Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used with catalysts deposited on a carrier
    • C10G47/12Inorganic carriers

Landscapes

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

Abstract

A methane-rich gas mixture is made by reacting with at least the minimum amount of hydrogen required for complete conversion to methane of the non-aromatic hydrocarbons present in the feedstock, in the presence of a fixed bed methanation catalyst, a hydrocarbon comprising liquefied propane and butane, or a petroleum distillate boiling up to 350 DEG C. The catalyst is preferably nickel or cobalt, optionally promoted by a precious metal of Group VIII and on a refractory support; e.g. the catalyst, before reduction, may comprise nickel chromite or cobalt chromite on a magnesia support, or nickel on alumina. The hydrogen may be provided by steam-reforming hydrocarbons, but the hydrogen-containing gas mixture should not contain more than 15% Co equivalent or more than 10% steam. Pressures of 0 to 750 p.s.i.g. are mentioned. Two specific examples are given. The product gas may be used to enrich a lean gas, e.g. water gas.ALSO:Three catalysts employed in a comparative example concerned with making a methane-rich gas by reacting hydrogen with a light petroleum distillate comprise:- nickel chromite comprising 52.6% NiO and 47.4% Cr2O3: nickel chromite on magnesia comprising 21.2% NiO, 17.8% Cr2O3, 0.4% Al2O3, 60.6% MgO; and coprecipitated nickel on alumina comprising 71.3% NiO, 28.7% Al2O3. Each catalyst was reduced with hydrogen at 450 DEG C.
GB5016563A 1963-12-19 1963-12-19 Making methane-rich gas Expired GB1111643A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB5016563A GB1111643A (en) 1963-12-19 1963-12-19 Making methane-rich gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB5016563A GB1111643A (en) 1963-12-19 1963-12-19 Making methane-rich gas

Publications (1)

Publication Number Publication Date
GB1111643A true GB1111643A (en) 1968-05-01

Family

ID=10454902

Family Applications (1)

Application Number Title Priority Date Filing Date
GB5016563A Expired GB1111643A (en) 1963-12-19 1963-12-19 Making methane-rich gas

Country Status (1)

Country Link
GB (1) GB1111643A (en)

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