GB1167492A - Steam Reforming Process - Google Patents

Steam Reforming Process

Info

Publication number
GB1167492A
GB1167492A GB6128/66A GB612866A GB1167492A GB 1167492 A GB1167492 A GB 1167492A GB 6128/66 A GB6128/66 A GB 6128/66A GB 612866 A GB612866 A GB 612866A GB 1167492 A GB1167492 A GB 1167492A
Authority
GB
United Kingdom
Prior art keywords
methanol
gas
stage
steam
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
GB6128/66A
Inventor
Richard John Young
Harold Watson
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 GB6128/66A priority Critical patent/GB1167492A/en
Priority to SE00912/67A priority patent/SE348704B/xx
Priority to DE19671645844 priority patent/DE1645844A1/en
Priority to FR92031A priority patent/FR1513633A/en
Priority to JP42004116A priority patent/JPS4827722B1/ja
Publication of GB1167492A publication Critical patent/GB1167492A/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
    • C01B3/32Production 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
    • 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
    • C01B3/38Production 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
    • 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
    • C10G11/00Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/10Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with stationary catalyst bed
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

1,167,492. Making combustible gas. IMPERIAL CHEMICAL INDUSTRIES Ltd. 9 Jan., 1967 [21 Jan., 1966; 7 Feb., 1966; 11 Feb., 1966], Nos. 2839/66, 5276/66 and 6128/66. Heading C5E. The output of a gas-making plant, e.g. for town or synthesis gas, in which a hydrocarbon is catalytically reacted with steam, is increased by gasifying methanol in part or complete substitution for, or in addition to, the normal feedstock, over one or more of the catalysts installed for normal operation of the plant. The methanol is preferably used simultaneously with one or both of a normally liquid hydrocarbon (A) and a normally gaseous hydrocarbon (B) having a higher hydrogen to carbon atomic ratio than A, e.g. B may be methane or natural gas, or a refinery gas, and the gas-making reaction may be performed in an externally heated tube reformer, or by a cyclic process, or by a partial combustion process. Multi-stage processes may be employed, e.g. the methanol may be fed to the hot gas produced by catalytically reacting A with steam, for reacting the mixture over a second catalyst, and in a modified form of the invention, the methanol is gasified in a vessel which succeeds the gasmaking stage, e.g. in a carbon monoxideconversion stage. This may be multi-stage, with the methanol injected before and/or between the stages, and a methanol synthesis catalyst may precede the operative conversion catalyst to reduce methane formation. Means for controlling the proportions of steam, feedstock and methanol delivered to the reaction zone are provided. An independent boiler may be provided to make up deficiencies in the usual waste heat boiler due to lowering of the temperature of the product gas caused by the methanol decomposition.
GB6128/66A 1966-01-21 1966-01-21 Steam Reforming Process Expired GB1167492A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
GB6128/66A GB1167492A (en) 1966-01-21 1966-01-21 Steam Reforming Process
SE00912/67A SE348704B (en) 1966-01-21 1967-01-20
DE19671645844 DE1645844A1 (en) 1966-01-21 1967-01-20 Steam reforming process
FR92031A FR1513633A (en) 1966-01-21 1967-01-20 Process for increasing the efficiency of a gasifier installation
JP42004116A JPS4827722B1 (en) 1966-01-21 1967-01-21

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB283966 1966-01-21
GB6128/66A GB1167492A (en) 1966-01-21 1966-01-21 Steam Reforming Process
GB527666 1966-02-07

Publications (1)

Publication Number Publication Date
GB1167492A true GB1167492A (en) 1969-10-15

Family

ID=27254133

Family Applications (1)

Application Number Title Priority Date Filing Date
GB6128/66A Expired GB1167492A (en) 1966-01-21 1966-01-21 Steam Reforming Process

Country Status (5)

Country Link
JP (1) JPS4827722B1 (en)
DE (1) DE1645844A1 (en)
FR (1) FR1513633A (en)
GB (1) GB1167492A (en)
SE (1) SE348704B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1767281C2 (en) * 1968-04-20 1975-04-10 Ruhrchemie Ag, 4200 Oberhausen-Holten Process for the catalytic cleavage of isobutyraldehyde
AT284784B (en) * 1968-11-19 1970-09-25 Ruhrchemie Ag Process for the production of a synthesis gas suitable for use in oxo synthesis
AR220381A1 (en) * 1979-04-16 1980-10-31 Sao Paulo Gas CATALYTIC PROCESS FOR THE GASIFICATION OF ETHANOL WITH STEAM

Also Published As

Publication number Publication date
DE1645844A1 (en) 1970-07-09
SE348704B (en) 1972-09-11
FR1513633A (en) 1968-02-16
JPS4827722B1 (en) 1973-08-25

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Legal Events

Date Code Title Description
PS Patent sealed
PE Patent expired