NL7111477A - Synthesis gas generation - by partial oxidn of hydrocarbon liquids - Google Patents

Synthesis gas generation - by partial oxidn of hydrocarbon liquids

Info

Publication number
NL7111477A
NL7111477A NL7111477A NL7111477A NL7111477A NL 7111477 A NL7111477 A NL 7111477A NL 7111477 A NL7111477 A NL 7111477A NL 7111477 A NL7111477 A NL 7111477A NL 7111477 A NL7111477 A NL 7111477A
Authority
NL
Netherlands
Prior art keywords
water
effluent
hydrocarbon
degrees
gas
Prior art date
Application number
NL7111477A
Other versions
NL169575B (en
NL169575C (en
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
Priority to NL7111477A priority Critical patent/NL169575C/en
Publication of NL7111477A publication Critical patent/NL7111477A/en
Publication of NL169575B publication Critical patent/NL169575B/en
Application granted granted Critical
Publication of NL169575C publication Critical patent/NL169575C/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/04Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
    • 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
    • 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
    • C01B3/48Production 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 followed by reaction of water vapour with carbon monoxide

Abstract

Synthesis gas (CO + H2) is made by non-catalytic process comprising partial oxidn. of liquid hydrocarbon fuels with oxygen-rich gas and steam. Process is economic in that steam generation is by cooling of effluent streams and hydrocarbon feed is used as a first scrubbing agent. Also, any oil loss in a second stage water scrubbing is recovered, and removal of carbon from quench water as in prior art processes is not required. Reaction is carried out in unpacked reactor at 1800-3000 degrees F. The effluent is first cooled to 400-550 degrees F (above dew point of water) by indirect heat exchange, and then scrubbed with 1-10 gals hydrocarbon fluid per 1000 cu. ft. gas (where fluid is fresh liquid hydrocarbon fuel) at temps. above the dew point of water in effluent gas to remove particulate carbon, followed by recycle of the fluid-carbon slurry as feedstock for the process. Also the effluent may be further scrubbed with water (1-10 gals/1000 cu. ft) at 100-500 degrees F to condense any hydrocarbon vapours, the liquid prod. then being heated and fed to the reaction zone. All process stages are operated at about equal press. in range 100-3000 psig.
NL7111477A 1971-08-20 1971-08-20 PROCESS FOR THE PREPARATION OF CARBON MONOXIDE AND HYDROGEN BY OXYDATION OF A LIQUID HYDROCARBON, REMOVING CARBONS PRESENT IN THE PRODUCT GAS BY USING A LIQUID HYDROCARBON. NL169575C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
NL7111477A NL169575C (en) 1971-08-20 1971-08-20 PROCESS FOR THE PREPARATION OF CARBON MONOXIDE AND HYDROGEN BY OXYDATION OF A LIQUID HYDROCARBON, REMOVING CARBONS PRESENT IN THE PRODUCT GAS BY USING A LIQUID HYDROCARBON.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL7111477A NL169575C (en) 1971-08-20 1971-08-20 PROCESS FOR THE PREPARATION OF CARBON MONOXIDE AND HYDROGEN BY OXYDATION OF A LIQUID HYDROCARBON, REMOVING CARBONS PRESENT IN THE PRODUCT GAS BY USING A LIQUID HYDROCARBON.

Publications (3)

Publication Number Publication Date
NL7111477A true NL7111477A (en) 1973-02-22
NL169575B NL169575B (en) 1982-03-01
NL169575C NL169575C (en) 1982-08-02

Family

ID=19813849

Family Applications (1)

Application Number Title Priority Date Filing Date
NL7111477A NL169575C (en) 1971-08-20 1971-08-20 PROCESS FOR THE PREPARATION OF CARBON MONOXIDE AND HYDROGEN BY OXYDATION OF A LIQUID HYDROCARBON, REMOVING CARBONS PRESENT IN THE PRODUCT GAS BY USING A LIQUID HYDROCARBON.

Country Status (1)

Country Link
NL (1) NL169575C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2300126A1 (en) * 1975-02-06 1976-09-03 Hoelter H PROCESS FOR PURIFYING THE GAS FORMED DURING THE CARBONATION OF PRESSURIZED COAL
EP2100945A1 (en) * 2008-03-12 2009-09-16 Aker Solutions US Inc. Process for removing tar from synthesis gas

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2300126A1 (en) * 1975-02-06 1976-09-03 Hoelter H PROCESS FOR PURIFYING THE GAS FORMED DURING THE CARBONATION OF PRESSURIZED COAL
EP2100945A1 (en) * 2008-03-12 2009-09-16 Aker Solutions US Inc. Process for removing tar from synthesis gas
US8470078B2 (en) 2008-03-12 2013-06-25 Ihi E&C International Corporation Process for removing tar from synthesis gas

Also Published As

Publication number Publication date
NL169575B (en) 1982-03-01
NL169575C (en) 1982-08-02

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Legal Events

Date Code Title Description
V1 Lapsed because of non-payment of the annual fee