GB236230A - Improvements in the process of hydrogenating tar oils - Google Patents
Improvements in the process of hydrogenating tar oilsInfo
- Publication number
- GB236230A GB236230A GB16523/25A GB1652325A GB236230A GB 236230 A GB236230 A GB 236230A GB 16523/25 A GB16523/25 A GB 16523/25A GB 1652325 A GB1652325 A GB 1652325A GB 236230 A GB236230 A GB 236230A
- Authority
- GB
- United Kingdom
- Prior art keywords
- temperature
- hydrogenation
- tar
- coke oven
- desulphurized
- 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
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
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
Tar oils are hydrogenated at ordinary pressure and elevated temperature using coke oven gas from which the water vapour has been removed. The coke oven gas is dehydrated by cooling, by calcium chloride or preferably by means of sulphuric acid, whilst the water formed during the reaction is vaporized at the temperature of the hydrogenation, viz. 180-200 DEG C., and carried away by the gas. The tar oils are previously desulphurized in known manner with ferrous sulphate or bog iron ore. An example is given of the hydrogenation of desulphurized tar oil in the presence of a colloidal nickel catalyst. The product may be treated at a temperature of 180-200 DEG C. with superheated steam to deprive it of its odour and colour. Specification 18998/12 is referred to.ALSO:Tar oils are hydrogenated at ordinary pressure and elevated temperature using coke oven gas from which the water vapour has been removed. The coke oven gas is dehydrated by cooling, by calcium chloride, or preferably by means of sulphuric acid, whilst the water formed during the reaction is vaporized at the temperature of the hydrogenation, viz. 180-200 DEG C., and carried away by the gas. The tar oils are previously desulphurized in known manner with ferrous sulphate or Rasen iron ore. An example is given of the hydrogenation of desulphurized tar fat oil in the presence of a colloidal nickel catalyst. The product may be treated at a temperature of 180-200 DEG C. with superheated steam to deprive it of its odour and colour. Specification 18998/12, [Class 1 (i), Chemical processes &c.], is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE236230X | 1924-06-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB236230A true GB236230A (en) | 1926-09-27 |
Family
ID=5900808
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB16523/25A Expired GB236230A (en) | 1924-06-30 | 1925-06-26 | Improvements in the process of hydrogenating tar oils |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB236230A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2422875A (en) * | 1942-08-17 | 1947-06-24 | Johnson & Co A | Process of refining hydrocarbons |
US2616834A (en) * | 1949-12-07 | 1952-11-04 | Sun Oil Co | Removal of objectionable sulfur compounds from mineral oil distillates |
-
1925
- 1925-06-26 GB GB16523/25A patent/GB236230A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2422875A (en) * | 1942-08-17 | 1947-06-24 | Johnson & Co A | Process of refining hydrocarbons |
US2616834A (en) * | 1949-12-07 | 1952-11-04 | Sun Oil Co | Removal of objectionable sulfur compounds from mineral oil distillates |
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