GB490768A - Improvements in the hydrogenation of polymerisation products of unsaturated hydrocarbons - Google Patents
Improvements in the hydrogenation of polymerisation products of unsaturated hydrocarbonsInfo
- Publication number
- GB490768A GB490768A GB536037A GB536037A GB490768A GB 490768 A GB490768 A GB 490768A GB 536037 A GB536037 A GB 536037A GB 536037 A GB536037 A GB 536037A GB 490768 A GB490768 A GB 490768A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stage
- catalyst
- stages
- immune
- preferably effected
- 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
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/02—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
- C07C5/03—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals of the platinum group metals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
- C07C2523/74—Iron group metals
- C07C2523/755—Nickel
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Polymerization products of unsaturated hydrocarbons are hydrogenated in two stages, in the first of which organic sulphur compounds are destroyed. The first stage is preferably effected with a catalyst immune from sulphur poisoning such as a metal of the 8th group, but alternatively a catalyst which has been partly poisoned by previous use in the second stage may be used. The catalyst used in the second stage may be liable to sulphur poisoning as, e.g. nickel, or immune as, e.g. the sulphides of 6th group metals. The first stage is preferably effected in a number of converters in parallel, and the second stage in a single converter. Between the stages impurities may be removed by washing with water or alkali. The reactions may be carried out in liquid or gaseous phase with or without increased pressure and usually at temperatures of 170-350 DEG C. The catalysts may be rigidly arranged, mounted on carriers, or suspended. Examples are given of the conversion of di-isobutylene into iso-octane using nickel catalysts. Specification 315,439, [Class 1 (i)], is referred to.ALSO:Polymerization products of unsaturated hydrocarbons are hydrogenated in two stages, in the first of which organic sulphur compounds are destroyed. The first stage is preferably effected with a catalyst immune from sulphur poisoning such as a metal of the 8th group, but alternatively a catalyst which has been partly poisoned by previous use in the second stage may be used. The catalyst used in the second stage may be liable to sulphur poisoning as, e.g. nickel, or immune as, e.g. sulphides of 6th group metals. The first stage is preferably effected in a number of converters in parallel and the second stage in a single converter. Between the stages impurities may be removed by washing with water or alkali. The reactions may be carried out in liquid or gaseous phase with or without pressure and usually at temperatures of 170-350 DEG C. The catalysts may be rigidly arranged, mounted on carriers, or suspended. Examples are given of the conversion of diisobutylene into iso-octane using nickel catalysts. Specification 315,439, [Class 2 (iii)], is referred to.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB536037A GB490768A (en) | 1937-02-23 | 1937-02-23 | Improvements in the hydrogenation of polymerisation products of unsaturated hydrocarbons |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB536037A GB490768A (en) | 1937-02-23 | 1937-02-23 | Improvements in the hydrogenation of polymerisation products of unsaturated hydrocarbons |
Publications (1)
Publication Number | Publication Date |
---|---|
GB490768A true GB490768A (en) | 1938-08-22 |
Family
ID=9794635
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB536037A Expired GB490768A (en) | 1937-02-23 | 1937-02-23 | Improvements in the hydrogenation of polymerisation products of unsaturated hydrocarbons |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB490768A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3324018A (en) * | 1963-09-30 | 1967-06-06 | Standard Oil Co | Hydrogenation method |
EP0255754A1 (en) * | 1986-07-31 | 1988-02-10 | Uop | Olefin hydrogenation method |
-
1937
- 1937-02-23 GB GB536037A patent/GB490768A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3324018A (en) * | 1963-09-30 | 1967-06-06 | Standard Oil Co | Hydrogenation method |
EP0255754A1 (en) * | 1986-07-31 | 1988-02-10 | Uop | Olefin hydrogenation method |
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