GB880108A - Reforming of gaseous hydrocarbons and liquid hydrocarbons of low boiling point - Google Patents
Reforming of gaseous hydrocarbons and liquid hydrocarbons of low boiling pointInfo
- Publication number
- GB880108A GB880108A GB591158A GB591158A GB880108A GB 880108 A GB880108 A GB 880108A GB 591158 A GB591158 A GB 591158A GB 591158 A GB591158 A GB 591158A GB 880108 A GB880108 A GB 880108A
- Authority
- GB
- United Kingdom
- Prior art keywords
- methane
- hydrocarbons
- steam
- catalyst
- reaction zone
- 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
- C01B3/32—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
- C01B3/384—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 the catalyst being continuously externally heated
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
- B01J8/062—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes being installed in a furnace
-
- 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
- C01B3/40—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 characterised by the catalyst
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Hydrogen, Water And Hydrids (AREA)
Abstract
Gaseous hydrocarbons and liquid hydrocarbons of low boiling point are converted into a gas containing hydrogen and carbon monoxide by passing the hydrocarbon in admixture with steam and/or carbon dioxide through an externally heated multi-tubular reaction zone containing a catalyst while maintaining at the outlet to the reaction zone a temperature between 1350 DEG and 1700 DEG F., preferably between 1450 DEG and 1600 DEG F., and a pressure of at least 50 p.s.i.g., preferably between 65 and 150 p.s.i.g., the steam to methane or methane equivalent mol. ratio being at least 1,8:1 and the space velocity corresponding to at least 700 volumes of methane or methane equivalent per hour per volume of catalyst. The hydrocarbon feed is preheated to between 400 DEG and 1250 DEG F., preferably between 800 DEG and 1150 DEG F., while the steam to methane or methane equivalent ratio is preferably between 2,1:1 and 2,6:1. The tubes of the reaction zone have an outside diameter of between 2 1/2 and 5 inches and the catalyst is preferably nickel oxide or nickel and calcium oxides on a silica-alumina support in the form of spheres or pellets having a diameter or length between 1/4 and inch. The hydrocarbons converted may be methane, ethane, propane, butane, natural gas, liquefied petroleum, gas or nephtha.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB591158A GB880108A (en) | 1958-02-24 | 1958-02-24 | Reforming of gaseous hydrocarbons and liquid hydrocarbons of low boiling point |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB591158A GB880108A (en) | 1958-02-24 | 1958-02-24 | Reforming of gaseous hydrocarbons and liquid hydrocarbons of low boiling point |
Publications (1)
Publication Number | Publication Date |
---|---|
GB880108A true GB880108A (en) | 1961-10-18 |
Family
ID=9804928
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB591158A Expired GB880108A (en) | 1958-02-24 | 1958-02-24 | Reforming of gaseous hydrocarbons and liquid hydrocarbons of low boiling point |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB880108A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3201214A (en) * | 1963-02-01 | 1965-08-17 | Pullman Inc | Production of domestic heating gas |
GB2170508A (en) * | 1985-01-17 | 1986-08-06 | Linde Ag | Production of H2/CO synthesis gas |
-
1958
- 1958-02-24 GB GB591158A patent/GB880108A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3201214A (en) * | 1963-02-01 | 1965-08-17 | Pullman Inc | Production of domestic heating gas |
GB2170508A (en) * | 1985-01-17 | 1986-08-06 | Linde Ag | Production of H2/CO synthesis gas |
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