GB970790A - Process for the preparation of primary alcohols - Google Patents
Process for the preparation of primary alcoholsInfo
- Publication number
- GB970790A GB970790A GB989962A GB989962A GB970790A GB 970790 A GB970790 A GB 970790A GB 989962 A GB989962 A GB 989962A GB 989962 A GB989962 A GB 989962A GB 970790 A GB970790 A GB 970790A
- Authority
- GB
- United Kingdom
- Prior art keywords
- catalyst
- weight
- cobalt
- catalysts
- thorium
- 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
-
- 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
- B01J23/90—Regeneration or reactivation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Primary alcohols are produced by hydrogenating a C7 to C22 aliphatic monoepoxide having a terminal epoxide group in the presence of a catalyst which contains at least 50% by weight of cobalt, iron or osmium or at least 50% by weight of a mixture thereof and optionally also containing at most 50% or preferably 35% by weight of nickel, referred to the metal in the catalyst; the hydrogenation may be effected at 100 to 250 DEG C. preferably 120 to 200 DEG C. at superatmospheric pressures up to 400 ats. There may also be present as activator a small amount of thorium, magnesium or alkali metal and the catalyst may be supported on a carrier e.g. aluminium oxide, aibieic acid or pumice. In the examples, which include the preparation of catalysts (see Division B1), the use of catalysts outside the scope of the invention is contrasted, and purification of the resulting products, which contain minor amounts of paraffins and secondary alcohols is effected by vacuum fractional distillation using a spinning band column. Batch and continuous hydrogenation over fixed beds of catalyst are described.ALSO:Catalysts containing at least 50% by weight of cobalt, iron or osmium metal or at least 50% by weight of a mixture thereof, and up to optionally 50%, preferably 35%, by weight of metals present of nickel are employed for hydrogenating aliphatic monoepoxides to primary alcohols (see Division C2). There may also be present, as activator, a small amount of thorium, magnesium or alkali metal and the catalyst may be supported on a solid carrier, e.g. aluminium oxide, silicic acid or pumice. In the examples there is described the detailed preparations of a cobalt catalyst containing magnesium and thorium by precipitating the carbonates on to kieselguhr, the final activation being carried out by reduction in hydrogen, and of a non supported, tabletted cobalt manganese catalyst. The use of other catalysts prepared by identical means or literature methods, as the case may be, is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEH0042223 | 1961-04-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB970790A true GB970790A (en) | 1964-09-23 |
Family
ID=7154786
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB989962A Expired GB970790A (en) | 1961-04-06 | 1962-03-15 | Process for the preparation of primary alcohols |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB970790A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3956405A (en) * | 1973-02-27 | 1976-05-11 | Daikin Kogyo Kabushiki Kaisha | Process for manufacturing polyfluoroalkyl propanols |
US4590313A (en) * | 1982-06-02 | 1986-05-20 | Atlantic Richfield Company | Method for producing primary alcohols by catalytic hydrogenation of terminal epoxides |
WO2002076610A1 (en) * | 2001-03-22 | 2002-10-03 | Showa Denko K. K. | Catalyst for producing both end-hydroxyl group-terminated diols, process for producing the catalyst, process for producing the diols by using the catalyst, and both end-hydroxyl group-terminated diols obtained by the process |
US6608235B1 (en) * | 1998-10-29 | 2003-08-19 | Ube Industries, Ltd. | Method of reducing epoxidized organic compound with hydrogen |
WO2013061515A1 (en) | 2011-10-27 | 2013-05-02 | 高砂香料工業株式会社 | Method for producing 3-menthoxy propanol and composition for imparting cooling sensation |
-
1962
- 1962-03-15 GB GB989962A patent/GB970790A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3956405A (en) * | 1973-02-27 | 1976-05-11 | Daikin Kogyo Kabushiki Kaisha | Process for manufacturing polyfluoroalkyl propanols |
US4590313A (en) * | 1982-06-02 | 1986-05-20 | Atlantic Richfield Company | Method for producing primary alcohols by catalytic hydrogenation of terminal epoxides |
US6608235B1 (en) * | 1998-10-29 | 2003-08-19 | Ube Industries, Ltd. | Method of reducing epoxidized organic compound with hydrogen |
WO2002076610A1 (en) * | 2001-03-22 | 2002-10-03 | Showa Denko K. K. | Catalyst for producing both end-hydroxyl group-terminated diols, process for producing the catalyst, process for producing the diols by using the catalyst, and both end-hydroxyl group-terminated diols obtained by the process |
US7230145B2 (en) | 2001-03-22 | 2007-06-12 | Showa Denko K.K. | Catalyst for producing both end-hydroxyl group-terminated diols, process for producing the catalyst, process for producing the diols by using the catalyst, and both end-hydroxyl group-terminated diols obtained by the process |
WO2013061515A1 (en) | 2011-10-27 | 2013-05-02 | 高砂香料工業株式会社 | Method for producing 3-menthoxy propanol and composition for imparting cooling sensation |
US20140328771A1 (en) * | 2011-10-27 | 2014-11-06 | Takasago International Corporation | Method for producing 3-menthoxy propanol and compositions for imparting cooling sensation |
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