GB454389A - Improvements in the manufacture and production of non-knocking motor fuel by the catalytic reaction of carbon monoxide and hydrogen - Google Patents
Improvements in the manufacture and production of non-knocking motor fuel by the catalytic reaction of carbon monoxide and hydrogenInfo
- Publication number
- GB454389A GB454389A GB1060835A GB1060835A GB454389A GB 454389 A GB454389 A GB 454389A GB 1060835 A GB1060835 A GB 1060835A GB 1060835 A GB1060835 A GB 1060835A GB 454389 A GB454389 A GB 454389A
- Authority
- GB
- United Kingdom
- Prior art keywords
- boiling
- fractions
- hydrogen
- carbon monoxide
- compression
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G50/00—Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
Abstract
Non-knocking motor fuels are manufactured from the hydrocarbons formed by the catalytic conversion of carbon monoxide with hydrogen, by treating the low-boiling constituents thereof, or their fractions rich in olefines, preferably after separation of the higher boiling constituents, at an elevated temperature, e.g. 20--250 DEG C., with condensing agents under such conditions of time, temperature and activity of catalyst that hydrocarbons boiling higher, but not substantially above the end boiling point of benzine, are formed. The gases and vapours from the conversion of carbon monoxide and hydrogen may first be freed from constituents of high boiling point, particularly those of higher boiling point than benzine, by cooling, the products of low boiling point then being separated, e.g. by compression, which may be in three or more stages. Thus, the gases may be compressed at 3, 8, 24 and, if desired, 50 atmospheres, the first two fractions being directly employed, preferably in admixture with low boiling benzine fractions, and the later fractions being subjected to the polymerizing treatment. The polymerized product is advantageously mixed with the higher boiling fractions separated in the first stage of the compression. Alternatively, the condensing treatment may be applied to the whole of the benzine obtained by compression, or by absorption or washing instead of compression, whilst olefines from other sources may also be added during the condensation. Suitable condensing agents are halogen, sulphur, or halides such as boron fluoride, aluminium chloride, zinc chloride, titanium chloride or tin chloride, or bleaching earths impregnated with phosphoric acid or halides, or mixtures thereof. In an example, a mixture of carbon monoxide and hydrogen is led at 190 DEG C. over a catalyst consisting of cobalt, manganese and kieselguhr, the product is cooled to remove constituents boiling above 180 DEG C., the remaining gaseous mixture compressed at 3, 8 and 24 atmospheres, and the two latter fractions treated at 235 DEG C. with bleaching earth impregnated with phosphoric acid.ALSO:Non-knocking motor fuels are manufactured from the hydrocarbons formed by the catalytic conversion of carbon monoxide with hydrogen, by treating the low - boiling constituents thereof at an elevated temperature with condensing agents. The gases and vapours from the conversion of carbon monoxide and hydrogen may first be freed from high - boiling constituents by cooling, the products of low boiling point then being separated, e.g. by compression, which may be in three or more stages. Thus the gases may be compressed at 3, 8, 24 and, if desired, 50 atmospheres, the first two fractions being directly employed, preferably in admixture with low - boiling benzine fractions, and the later fractions being subjected to the polymerizing treatment. The polymerized product is advantageously mixed with the higher-boiling fractions separated in the first stage of the compression.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1060835A GB454389A (en) | 1935-04-05 | 1935-04-05 | Improvements in the manufacture and production of non-knocking motor fuel by the catalytic reaction of carbon monoxide and hydrogen |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1060835A GB454389A (en) | 1935-04-05 | 1935-04-05 | Improvements in the manufacture and production of non-knocking motor fuel by the catalytic reaction of carbon monoxide and hydrogen |
Publications (1)
Publication Number | Publication Date |
---|---|
GB454389A true GB454389A (en) | 1936-09-30 |
Family
ID=9970983
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1060835A Expired GB454389A (en) | 1935-04-05 | 1935-04-05 | Improvements in the manufacture and production of non-knocking motor fuel by the catalytic reaction of carbon monoxide and hydrogen |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB454389A (en) |
-
1935
- 1935-04-05 GB GB1060835A patent/GB454389A/en not_active Expired
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