GB407127A - Improved process for the treatment with hydrogenating gases of distillable carbonaceous materials - Google Patents
Improved process for the treatment with hydrogenating gases of distillable carbonaceous materialsInfo
- Publication number
- GB407127A GB407127A GB3023332A GB3023332A GB407127A GB 407127 A GB407127 A GB 407127A GB 3023332 A GB3023332 A GB 3023332A GB 3023332 A GB3023332 A GB 3023332A GB 407127 A GB407127 A GB 407127A
- Authority
- GB
- United Kingdom
- Prior art keywords
- rhenium
- hydrogen
- disulphide
- active carbon
- catalyst
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/32—Manganese, technetium or rhenium
- B01J23/36—Rhenium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/28—Molybdenum
-
- 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
- C10G47/02—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions characterised by the catalyst used
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
In the treatment of distillable carbonacous materials containing at least three carbon atoms in the molecule with hydrogen at elevated temperatures and preferably under pressure, the carbonaceous materials and a catalyst containing rhenium are passed together with the hydrogenating gases through the reaction vessel. The rhenium catalyst may be applied to the material in solution, as a colloidal suspension, or the material may be impregnated therewith. Rhenium sulphides, oxides, halides, or perrhenates are mentioned and the rhenium compound may be applied to a carrier, e.g. florida earth, active carbon or coke activated by steam or acids. Regeneration of the catalyst may be obtained by the addition of liquid oxidising agents, e.g. nitric acid. Naphthalene mixed with rhenium sulphide prepared as described below is passed with hydrogen through a vessel maintained at 440 DEG C. and 180 atmospheres pressure. A liquid hydrogenated product is obtained containing decahydro and tetrahydronaphthalene. Benzene is similarly converted to cyclohexane. Cylinder oil is treated with molybdic acid and rhenium heptasulphide absorbed on active carbon and a lubricating p oil boiling above 360 C. is obtained, while cresol is converted into benzines in presence of rhenium disulphide. Rhenium disulphide is obtained by dissolving potassium perrhenate in water and passing in hydrogen sulphide slowly. The solution is acidified with hydrogen chloride and the black precipitate of the heptasulphide is further treated in a tube at 400 DEG C. with hydrogen sulphide to convert it into the disulphide. The treatment may take place in the presence of active carbon. Specifications 379,587 and 379,755 are referred to.ALSO:In the treatment of distillable carbonaceous materials containing at least three carbon atoms in the molecule with hydrogen at elevated temperatures and preferably under pressure, the carbonaceous materials and a catalyst containing rhenium are passed together with the hydrogenating gases through the reaction vessel. The rhenium catalyst may be applied to the material in solution, as a colloidal suspension, or the material may be impregnated therewith. Rhenium sulphides, oxides, halides, or perrhenates are mentioned and the rhenium compound may be applied to a carrier, e.g. florida earth, active carbon or coke activated by steam or acids. Regeneration of the catalyst may be obtained by the addition of liquid oxidizing agents, e.g. nitric acid. Naphthalene mixed with rhenium sulphide prepared as described below is passed with hydrogen through a vessel maintained at 440 DEG C. and 180 atmospheres pressure. A liquid hydrogenated product is obtained containing decahydro and tetrahydronaphthalene. Benzene is similarly converted to cyclohexane. Cylinder oil is treated with molybdic acid and rhenium heptasulphide absorbed on active carbon and a lubricating oil boiling above 360 DEG C. is obtained, while cresol is converted into benzines in presence of rhenium disulphide. Rhenium disulphide is obtained by dissolving potassium perrhenate in water and passing in hydrogen sulphide slowly. The solution is acidified with hydrogen chloride and the black precipitate of the heptasulphide is further treated in a tube at 400 DEG C. with hydrogen sulphide to convert it into the disulphide. The treatment may take place in the presence of active carbon. Specifications 379,587, and 379,755, [Group III], are referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3023332A GB407127A (en) | 1932-10-28 | 1932-10-28 | Improved process for the treatment with hydrogenating gases of distillable carbonaceous materials |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB3023332A GB407127A (en) | 1932-10-28 | 1932-10-28 | Improved process for the treatment with hydrogenating gases of distillable carbonaceous materials |
Publications (1)
Publication Number | Publication Date |
---|---|
GB407127A true GB407127A (en) | 1934-03-15 |
Family
ID=10304394
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB3023332A Expired GB407127A (en) | 1932-10-28 | 1932-10-28 | Improved process for the treatment with hydrogenating gases of distillable carbonaceous materials |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB407127A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3512915A1 (en) * | 1984-04-13 | 1985-10-17 | Deutsche Bp Ag, 2000 Hamburg | Process for the hydroconversion of sulphur-containing heavy hydrocarbons |
US4560803A (en) * | 1982-09-21 | 1985-12-24 | Exxon Research & Engineering Co. | Catalysts and process for oxidation of olefins to ketones |
US4737482A (en) * | 1983-07-25 | 1988-04-12 | Exxon Research & Engineering Co. | Catalysts for oxidation of olefins to ketones |
US4876392A (en) * | 1982-09-21 | 1989-10-24 | Exxon Research & Engineering Company | Process for preparation of keystones by oxidation of secondary alcohols using a trimetallic catalyst comprising molybdenum, rhenium and a group VIII noble metal |
-
1932
- 1932-10-28 GB GB3023332A patent/GB407127A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4560803A (en) * | 1982-09-21 | 1985-12-24 | Exxon Research & Engineering Co. | Catalysts and process for oxidation of olefins to ketones |
US4876392A (en) * | 1982-09-21 | 1989-10-24 | Exxon Research & Engineering Company | Process for preparation of keystones by oxidation of secondary alcohols using a trimetallic catalyst comprising molybdenum, rhenium and a group VIII noble metal |
US4737482A (en) * | 1983-07-25 | 1988-04-12 | Exxon Research & Engineering Co. | Catalysts for oxidation of olefins to ketones |
DE3512915A1 (en) * | 1984-04-13 | 1985-10-17 | Deutsche Bp Ag, 2000 Hamburg | Process for the hydroconversion of sulphur-containing heavy hydrocarbons |
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