GB686247A - Manufacture of primary alcohols - Google Patents
Manufacture of primary alcoholsInfo
- Publication number
- GB686247A GB686247A GB152050A GB152050A GB686247A GB 686247 A GB686247 A GB 686247A GB 152050 A GB152050 A GB 152050A GB 152050 A GB152050 A GB 152050A GB 686247 A GB686247 A GB 686247A
- Authority
- GB
- United Kingdom
- Prior art keywords
- isomerization
- hydrogen
- over
- hydrogenation
- pentanol
- 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
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/14—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group
- C07C29/141—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of a —CHO group with hydrogen or hydrogen-containing gases
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/56—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds from heterocyclic compounds
- C07C45/57—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds from heterocyclic compounds with oxygen as the only heteroatom
- C07C45/58—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds from heterocyclic compounds with oxygen as the only heteroatom in three-membered rings
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Primary alcohols are made by passing an epoxide of formula <FORM:0686247/IV (b)/1> in which R1 and R2 are alkyl, aryl or alicyclic radicals, in the vapour phase at elevated temperatures over an isomerization catalyst until substantially complete conversion to the corresponding aldehyde has taken place and subsequently conducting the mixture from the isomerization step with hydrogen over a hydrogenation catalyst at elevated temperatures. Substantially complete conversion is defined as such as results in the vapours leaving the isomerization reactor having no more than 5 per cent of the initial amount of epoxide. Isomerization is preferably effected with inert gases, hydrogen being preferred since it may be used in the subsequent hydrogenation. Many epoxides are specified representative being isobutene oxide and alpha-methylstyrene oxide and the oxides of propylene dimer 2,3,4-trimethyl pentene-1 and cyclohexyl-methyl-ethylene. The reaction mixture obtained by treating alpha-di-isobutene in the liquid phase with molecular oxygen in the presence of oxidation catalysts, cf. Specification 682,067, may also be used. Alumina, expecially when activated, is the preferred isomerization catalyst and silica gel and phosphoric acid on carriers are also mentioned. Isomerization temperatures mentioned are 200-350 DEG C. and preferably the diluent gas is present in amounts to maintain the temperature at about 350 DEG C. Copper catalysts are preferred in the hydrogenation and temperatures specified are 180-350 DEG C. Hydrogen, which may be used in excess, e.g. 5-10 fold, may be recycled. In examples: (1) 1,2-epoxy-2,4,4-trimethyl pentane is passed with nitrogen over activated alumina and the pentanol obtained hydrogenated over copper on kieselguhr to the pentanol; (2) air oxidized di-isobutene is passed with hydrogen over activated alumina and the products over copper on kieselguhr to yield 2,4,4-trimethyl pentanol which is separated from methyl p neo-pentyl carbinol and ketone which are also obtained and (3) is similar to (2) save that extra hydrogen is provided for the hydrogenation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB152050A GB686247A (en) | 1950-01-20 | 1950-01-20 | Manufacture of primary alcohols |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB152050A GB686247A (en) | 1950-01-20 | 1950-01-20 | Manufacture of primary alcohols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB686247A true GB686247A (en) | 1953-01-21 |
Family
ID=9723392
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB152050A Expired GB686247A (en) | 1950-01-20 | 1950-01-20 | Manufacture of primary alcohols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB686247A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0226242A1 (en) * | 1985-12-03 | 1987-06-24 | Shell Internationale Researchmaatschappij B.V. | Downflow isomerization of epoxides |
-
1950
- 1950-01-20 GB GB152050A patent/GB686247A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0226242A1 (en) * | 1985-12-03 | 1987-06-24 | Shell Internationale Researchmaatschappij B.V. | Downflow isomerization of epoxides |
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