GB665575A - A process for desulphurising hydrocarbon oils - Google Patents
A process for desulphurising hydrocarbon oilsInfo
- Publication number
- GB665575A GB665575A GB27438/49A GB2743849A GB665575A GB 665575 A GB665575 A GB 665575A GB 27438/49 A GB27438/49 A GB 27438/49A GB 2743849 A GB2743849 A GB 2743849A GB 665575 A GB665575 A GB 665575A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hydrogen
- litres
- temperature
- pressure
- 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
- 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
- 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
- C10G45/24—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 with hydrogen-generating compounds
- C10G45/28—Organic compounds; Autofining
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)
- Catalysts (AREA)
Abstract
Hydrocarbon oils boiling above 300 DEG C are desulphurized by treatment with a gas containing free hydrogen at a temperature above 200 DEG C and under a pressure of at least 10 atmospheres in the presence of a stationary catalyst, by letting the oils flow in a thin layer over the catalyst in a reaction space through which the gas containing free hydrogen is passed as a single continuous phase, the quantity of hydrogen discharged from the reaction space (calculated at normal temperature and pressure) being at most 500 litres, but preferably more than 50 litres, per kgm. of initial material. The gas may be pure hydrogen or hydrogen mixed with other gases, such as hydrocarbons, nitrogen and carbon oxides. A temperature of 250 DEG -450 DEG C may be used. In an example, a fraction obtained from crude oil by flash distillation (calculated boiling point 300-500 DEG C), is caused to flow as a thin film over a cobalt molybdate catalyst supported on alumina at a temperature of 370 DEG C and a pressure of 50 atms.; 250 litres of gas (measured after removal of hydrogen sulphide) per kgm. of oil supplied is discharged at the bottom of the reactor. The treated oil may be thermally or catalytically cracked, or destructively hydrogenated.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL665575X | 1948-12-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB665575A true GB665575A (en) | 1952-01-23 |
Family
ID=19798734
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB27438/49A Expired GB665575A (en) | 1948-12-24 | 1949-10-25 | A process for desulphurising hydrocarbon oils |
Country Status (2)
Country | Link |
---|---|
GB (1) | GB665575A (en) |
NL (1) | NL74348C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1132276B (en) * | 1957-03-15 | 1962-06-28 | Exxon Research Engineering Co | Process for the production of heat-resistant jet fuels |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1132278B (en) * | 1957-12-13 | 1962-06-28 | Bataafsche Petroleum | Process for the recovery of hydrogen from a reaction mixture |
-
0
- NL NL74348D patent/NL74348C/xx active
-
1949
- 1949-10-25 GB GB27438/49A patent/GB665575A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1132276B (en) * | 1957-03-15 | 1962-06-28 | Exxon Research Engineering Co | Process for the production of heat-resistant jet fuels |
Also Published As
Publication number | Publication date |
---|---|
NL74348C (en) |
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