GB855501A - Improvements in the conversion of oils, their fractions or residues with amounts of oxygen insufficient for complete combustion to form gases containing carbon monoxide and hydrogen - Google Patents
Improvements in the conversion of oils, their fractions or residues with amounts of oxygen insufficient for complete combustion to form gases containing carbon monoxide and hydrogenInfo
- Publication number
- GB855501A GB855501A GB27207/57A GB2720757A GB855501A GB 855501 A GB855501 A GB 855501A GB 27207/57 A GB27207/57 A GB 27207/57A GB 2720757 A GB2720757 A GB 2720757A GB 855501 A GB855501 A GB 855501A
- Authority
- GB
- United Kingdom
- Prior art keywords
- vaporizable
- fraction
- fractions
- residues
- oxygen
- 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
Links
Classifications
-
- 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
- C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
- C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
- C01B3/28—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using moving solid particles
- C01B3/30—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using moving solid particles using the fluidised bed technique
-
- 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
- C01B3/38—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 catalysts
- C01B3/386—Catalytic partial combustion
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/025—Processes for making hydrogen or synthesis gas containing a partial oxidation step
- C01B2203/0261—Processes for making hydrogen or synthesis gas containing a partial oxidation step containing a catalytic partial oxidation step [CPO]
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
- C01B2203/1047—Group VIII metal catalysts
- C01B2203/1052—Nickel or cobalt catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1258—Pre-treatment of the feed
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
855,501. Combustible gases. BADISCHE ANILIN- & SODA-FABRIK A.G. Aug. 29, 1957 [Sept. 8, 1956], No. 27207/57. Drawings to Specification. Class 55 (2). In a process wherein gases containing carbon monoxide and hydrogen are produced by partial combustion of oils, their fractions or residues, or bars and pitches containing non-vaporizable residues, the starting material is first converted by a thermal treatment into a vaporous and/or a vaporizable fraction and a non-vaporizable fraction and the non-vaporizable fraction is reacted with oxygen, optionally in the presence of steam and/or carbon dioxide, to form a hot carrier gas into which the vaporous and/or vaporizable fraction is introduced, the mixture being led into a fluidized layer of a catalyst at a temperature between 700 and 1200 C., preferably between 800 and 1000 C., without the supply of external heat. Suitable catalysts are elements of the 8th group of the Periodic Table, especially nickel, associated with refractory porous materials such as magnesite, chamotte or other siliceous materials. Compounds of elements of the 1st and/or the 2nd group of the Periodic Table and/or of the metals of the iron group may be introduced into the zone where the non-vaporizable fraction is being reacted to inhibit the formation of carbon black. The thermal treatment of the first stage may be a distillation, if necessary in the presence of steam and/or carbon dioxide, at temperatures up to 380 C., or it may be a mild thermal decomposition under pressure at temperatures between 400 and 530 C. In the case of tars and pitches the thermal treatment may be cracking to vaporous products and coke at temperatures between 400 and 600 C. Solid non- vaporizable fractions are preferably ground before being reacted with oxygen. If this fraction amounts to 25% of the initial material the amount of oxygen employed in the second stage is at least sufficient for complete combustion.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEB41681A DE1023016B (en) | 1956-09-08 | 1956-09-08 | Process for the conversion of oils with insufficient amounts of oxygen for complete combustion to carbon oxide and hydrogen |
Publications (1)
Publication Number | Publication Date |
---|---|
GB855501A true GB855501A (en) | 1960-11-30 |
Family
ID=6966483
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB27207/57A Expired GB855501A (en) | 1956-09-08 | 1957-08-29 | Improvements in the conversion of oils, their fractions or residues with amounts of oxygen insufficient for complete combustion to form gases containing carbon monoxide and hydrogen |
Country Status (3)
Country | Link |
---|---|
US (1) | US3090684A (en) |
DE (1) | DE1023016B (en) |
GB (1) | GB855501A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1292634B (en) * | 1957-09-24 | 1969-04-17 | Celleco Ab | Process for the production of highly concentrated gaseous oxides |
DE1144239B (en) * | 1959-09-01 | 1963-02-28 | Basf Ag | Process for the conversion of gaseous and liquid, sulfur-containing hydrocarbons, especially minerals, to hydrogen and carbon oxide |
DE1129134B (en) * | 1960-07-26 | 1962-05-10 | Basf Ag | Process for the catalytic conversion of liquid, sulphurous hydrocarbons with insufficient amounts of oxygen for complete combustion to form carbon oxide and hydrogen using fluidized beds consisting of catalyst bodies |
US3506417A (en) * | 1966-05-13 | 1970-04-14 | Phillips Petroleum Co | Hydrocarbon reforming |
US3481987A (en) * | 1967-08-14 | 1969-12-02 | Union Oil Co | Removal of oxygen impurity from carbon monoxide |
GB8426344D0 (en) * | 1984-10-18 | 1984-11-21 | British Petroleum Co Plc | Conversion process |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2378116A (en) * | 1941-07-10 | 1945-06-12 | Phillips Petroleum Co | Method and apparatus for control of vapor pressure |
US2697655A (en) * | 1947-12-31 | 1954-12-21 | Kellogg M W Co | Manufacture of a hydrogen-rich gas |
US2707147A (en) * | 1948-02-07 | 1955-04-26 | Hercules Powder Co Ltd | Production of domestic gas |
US2630378A (en) * | 1949-07-23 | 1953-03-03 | Texaco Development Corp | Generation of synthesis gas |
FR1028172A (en) * | 1950-11-04 | 1953-05-20 | Lummus Co | Improvements in the distillation of hydrocarbons |
US2716597A (en) * | 1951-06-12 | 1955-08-30 | Koppers Co Inc | Method and apparatus for the production of combustible gases from liquid fuels |
DE923843C (en) * | 1952-01-06 | 1955-02-21 | Basf Ag | Process for the generation of fuel, in particular synthesis gases, from gaseous or liquid fuels and lump fuels |
US2828196A (en) * | 1954-04-30 | 1958-03-25 | United Gas Improvement Co | Method of producing combustible gas rich in oil gas |
DE1070771B (en) * | 1956-10-10 |
-
1956
- 1956-09-08 DE DEB41681A patent/DE1023016B/en active Pending
-
1957
- 1957-08-29 GB GB27207/57A patent/GB855501A/en not_active Expired
- 1957-09-04 US US681945A patent/US3090684A/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
DE1023016B (en) | 1958-01-23 |
US3090684A (en) | 1963-05-21 |
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