GB710339A - Improvements in or relating to the synthesis of hydrocarbons and catalysts therefor - Google Patents
Improvements in or relating to the synthesis of hydrocarbons and catalysts thereforInfo
- Publication number
- GB710339A GB710339A GB11695/50A GB1169550A GB710339A GB 710339 A GB710339 A GB 710339A GB 11695/50 A GB11695/50 A GB 11695/50A GB 1169550 A GB1169550 A GB 1169550A GB 710339 A GB710339 A GB 710339A
- Authority
- GB
- United Kingdom
- Prior art keywords
- iron
- catalyst
- synthesis
- per cent
- gas
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/02—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
- C07C1/04—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
- C07C1/0425—Catalysts; their physical properties
- C07C1/043—Catalysts; their physical properties characterised by the composition
- C07C1/0435—Catalysts; their physical properties characterised by the composition containing a metal of group 8 or a compound thereof
- C07C1/044—Catalysts; their physical properties characterised by the composition containing a metal of group 8 or a compound thereof containing iron
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/18—Carbon
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/745—Iron
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/20—Carbon compounds
- C07C2527/232—Carbonates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
Abstract
Olefinic hydrocarbons are produced from a synthesis gas containing CO and H2 and substantial amounts of N2 by contacting at 450-650 DEG , preferably 550-650 DEG F., and 50-100, preferably 55-75 p.s.i.g., with a dense turbulent fluidized catalyst comprising iron on active carbon and promoted with an alkali metal compound. Such catalysts give H2/CO consumption ratios greater than the ratio in the feed whereby a once-through operation can be used with synthesis gas obtained by partial oxidation of natural gas and having a H2/CO ratio of 2 : 1. In view of the low pressure required, the synthesis gas may be produced by oxidation of coal or natural gas with air at similar low pressures. The synthesis may be effected with a gas throughput of 2-20 c.ft./lb. of catalyst/hr. at a linear velocity of 0.1-3 ft./sec. The preferred catalysts comprise 10-20 per cent reduced iron and 0.4-1 per cent promoter, e.g. potassium carbonate. The iron is distributed over the active carbon as by impregnation or by thermal decomposition of iron carbonyl. Natural gas is oxidized with air at 2000-2500 DEG F., the lower part of the reactor containing a reforming catalyst such as nickel or copper on alumina to convert any CO2 and H2O formed back to methane. The synthesis gas passes to a reactor containing powdered catalyst which is fluidized by the upward flow of gas. Liquid products are separated while the gaseous hydrocarbons may be recovered by adsorption in active carbon also in fluidized form. Where synthesis gas is obtained from coal, a further conversion to increase the H2/CO ratio from 1/1 to 2/1 may be effected. Examples illustrate the effect of varying the promoter (K2CO3) content. Other promoters may be used, e.g. potassium hydroxide, acetate or fluoride. Specification 649,464, [Group III], is referred to.ALSO:A catalyst for the synthesis of hydrocarbons from CO and H2 comprises iron or active carbon promoted with an alkaline metal compound, and in finely divided form, for example 100-400, preferably 150-200 mesh, suitable for fluidization. The preferred catalyst contains 10-20, especially 15 per cent. reduced iron, and 0.4-1, especially 0.4-0.6 per cent. potassium carbonate, the iron being distributed over the carbon carrier as by impregnation or decomposition of the carbonyl. Other promoters include potassium hydroxide, acetate, and fluoride. The promoter content depends upon the iron surface area and examples illustrate the variation in product quality with contents below and above an optimum 0.5 per cent. Specification 649,464 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US710339XA | 1949-06-16 | 1949-06-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB710339A true GB710339A (en) | 1954-06-09 |
Family
ID=22098847
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB11695/50A Expired GB710339A (en) | 1949-06-16 | 1950-05-10 | Improvements in or relating to the synthesis of hydrocarbons and catalysts therefor |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB710339A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2204055A (en) * | 1987-04-29 | 1988-11-02 | Shell Int Research | Process for the preparation of hydrocarbons |
EP2314557A1 (en) * | 2009-10-23 | 2011-04-27 | Netherlands Organisation for Scientific Research (Advanced Chemical Technologies for Sustainability) | Production of lower olefins from synthesis gas |
-
1950
- 1950-05-10 GB GB11695/50A patent/GB710339A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2204055A (en) * | 1987-04-29 | 1988-11-02 | Shell Int Research | Process for the preparation of hydrocarbons |
GB2204055B (en) * | 1987-04-29 | 1992-01-02 | Shell Int Research | Process for the preparation of hydrocarbons |
EP2314557A1 (en) * | 2009-10-23 | 2011-04-27 | Netherlands Organisation for Scientific Research (Advanced Chemical Technologies for Sustainability) | Production of lower olefins from synthesis gas |
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