NL7111477A - Synthesis gas generation - by partial oxidn of hydrocarbon liquids - Google Patents
Synthesis gas generation - by partial oxidn of hydrocarbon liquidsInfo
- 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
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
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
-
- 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
- C01B3/36—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 oxygen or mixtures containing oxygen as gasifying agents
-
- 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
- C01B3/48—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 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.
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)
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 |
-
1971
- 1971-08-20 NL NL7111477A patent/NL169575C/en not_active IP Right Cessation
Cited By (3)
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 |