GB427905A - Process for the production of motor fuel - Google Patents
Process for the production of motor fuelInfo
- Publication number
- GB427905A GB427905A GB3475333A GB3475333A GB427905A GB 427905 A GB427905 A GB 427905A GB 3475333 A GB3475333 A GB 3475333A GB 3475333 A GB3475333 A GB 3475333A GB 427905 A GB427905 A GB 427905A
- Authority
- GB
- United Kingdom
- Prior art keywords
- fraction
- boiling
- catalyst
- refining
- hydrogenation
- 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
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
- C10G45/02—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds to eliminate hetero atoms without changing the skeleton of the hydrocarbon involved and without cracking into lower boiling hydrocarbons; Hydrofinishing
-
- 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
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
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)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
A non-knocking motor fuel boiling between 130 and 240 DEG C., is produced by first dividing a hydrocarbon mixture, consisting largely of aromatic hydrocarbons, into a lower fraction and a fraction at least 80 per cent of which boils between 150 and 240 DEG C., and then subjecting the higher fraction to a refining, catalytic hydrogenation under pressure, in the presence of a catalyst comprising a metal compound and at a temperature below 390 DEG C. As initial materials, benzols or benzines obtained from coal tars may be employed. As catalysts, there may be used compounds, e.g. oxides, hydroxides, sulphides, halides and carbonates, of the metals of the sixth group, especially molybdenum, tungsten, chromium and uranium, and of strontium, vanadium manganese, rhenium, titanium, zirconium, zinc, cadmium, aluminium and cobalt. The catalyst may be deposited on carriers, preferably in the colloidal condition. The pressures employed may vary between 20 and 1000 atmospheres and the temperatures may lie between 200 and 390 DEG C, preferably 300 or 340--390 DEG C. Hydrogen alone or mixed with other gases e.g. nitrogen, carbon monoxide or dioxide, hydrogen sulphide, water vapour or methane, and the quantity may vary from 300 to 2000 cubic metres per ton of hydrocarbon treated which may be in the vapour phase. In a preferred method, a hydrocarbon mixture consisting mainly of aromatic hydrocarbons, e.g. crude or heavy benzol, is divided into two fractions, one boiling below 130 DEG C. and the other above, the second fraction being subjected to a refining hydrogenation and the first fraction to a chemical refining, e.g. with sulphuric acid. The products may be blended with other motor fuels, e.g. benzine. In an example, crude benzol is divided by distillation into a lower fraction boiling up to 160 DEG C., and a higher fraction boiling between 160--220 DEG C. The higher fraction is passed with hydrogen under a pressure of 200 atmospheres and at a temperature of 370 DEG C., over a catalyst comprising molybdic acid, zinc oxide and magnesia the conditions being such that no substantial splitting or hydrogenation of the aromatic nuclei takes place. A purified heavy benzol of boiling range 150--225 DEG C., is obtained. Specifications 349,655 and 372,783 are referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3475333A GB427905A (en) | 1933-12-11 | 1933-12-11 | Process for the production of motor fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3475333A GB427905A (en) | 1933-12-11 | 1933-12-11 | Process for the production of motor fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
GB427905A true GB427905A (en) | 1935-05-02 |
Family
ID=10369543
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3475333A Expired GB427905A (en) | 1933-12-11 | 1933-12-11 | Process for the production of motor fuel |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB427905A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2419029A (en) * | 1941-04-11 | 1947-04-15 | Phillips Petroleum Co | Process for desulfurizing and reforming hydrocarbons |
DE1264657B (en) * | 1954-12-30 | 1968-03-28 | California Research Corp | Process for increasing the octane number of petroleum distillates with boiling ranges between 80 and 260 |
-
1933
- 1933-12-11 GB GB3475333A patent/GB427905A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2419029A (en) * | 1941-04-11 | 1947-04-15 | Phillips Petroleum Co | Process for desulfurizing and reforming hydrocarbons |
DE1264657B (en) * | 1954-12-30 | 1968-03-28 | California Research Corp | Process for increasing the octane number of petroleum distillates with boiling ranges between 80 and 260 |
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