GB1114563A - Epoxidation process - Google Patents
Epoxidation processInfo
- Publication number
- GB1114563A GB1114563A GB2372865A GB2372865A GB1114563A GB 1114563 A GB1114563 A GB 1114563A GB 2372865 A GB2372865 A GB 2372865A GB 2372865 A GB2372865 A GB 2372865A GB 1114563 A GB1114563 A GB 1114563A
- Authority
- GB
- United Kingdom
- Prior art keywords
- hydroperoxide
- preferred
- reaction
- cumene
- alcohol
- 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
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
- C07D301/19—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with organic hydroperoxides
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Epoxy Compounds (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Epoxy compounds are prepared by reacting an olefinically unsaturated compound with a hydroperoxide of an aralkane, having at least one hydrogen atom on a carbon atom adjacent to the aromatic ring, in the liquid phase in the presence of a metal epoxidation catalyst, the amount of hydroperoxide employed being 0.1-1.0 mol per mol olefinic groups and the reaction being continued until hydroperoxide conversion is at least 95%. It is preferred to continue the reaction until hydroperoxide conversion is at least 98%. The preferred epoxidation catalysts are V, W, Mo and Se, particularly compounds thereof which are soluble in the reaction mixture, e.g. carboxylates. Preferred hydroperoxides are those of cumene and ethyl-benzene. Specified olefinic reactants include olefins, alcohols, esters, ethers, ketones and organic halides. The preferred olefinic group: hydroperoxide ratios are in the range 2:1 to 5:1. It is preferred to operate at - 10 DEG C. to 175 DEG C. in the presence of an organic solvent. In the course of the reaction, the hydroperoxide is reduced to an alcohol having the same carbon skeleton. This alcohol can be recovered and reacted with hydrogen to effect reduction to the corresponding hydrocarbon which on reaction with molecular oxygen yields the hydroperoxide which may be recycled. Examples relate to the preparation of propylene oxide using cumene hydroperoxide, which is prepared by oxidation of cumene. Cumyl alcohol is obtained as a by-product.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US37531064A | 1964-06-15 | 1964-06-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1114563A true GB1114563A (en) | 1968-05-22 |
Family
ID=23480369
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2372865A Expired GB1114563A (en) | 1964-06-15 | 1965-06-03 | Epoxidation process |
Country Status (11)
Country | Link |
---|---|
BE (1) | BE665177A (en) |
CH (1) | CH451897A (en) |
DE (1) | DE1518996A1 (en) |
DK (1) | DK129932B (en) |
ES (1) | ES314229A1 (en) |
FR (1) | FR1459795A (en) |
GB (1) | GB1114563A (en) |
IL (1) | IL23724A (en) |
LU (1) | LU48808A1 (en) |
NL (1) | NL6507186A (en) |
SE (1) | SE342447B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1209155A1 (en) * | 2000-11-20 | 2002-05-29 | Degussa AG | Process for the preparation of propylene oxide free of coupling products |
CN110483445A (en) * | 2019-08-28 | 2019-11-22 | 无锡智归科技有限公司 | The dewatering process of cumyl hydroperoxide and isopropylbenzene in a kind of production of propylene oxide device and its production process |
-
1965
- 1965-06-03 GB GB2372865A patent/GB1114563A/en not_active Expired
- 1965-06-04 NL NL6507186A patent/NL6507186A/xx unknown
- 1965-06-09 BE BE665177D patent/BE665177A/xx unknown
- 1965-06-10 LU LU48808D patent/LU48808A1/xx unknown
- 1965-06-14 FR FR20653A patent/FR1459795A/en not_active Expired
- 1965-06-14 IL IL2372465A patent/IL23724A/en unknown
- 1965-06-14 DK DK298365A patent/DK129932B/en unknown
- 1965-06-15 DE DE19651518996 patent/DE1518996A1/en active Pending
- 1965-06-15 ES ES0314229A patent/ES314229A1/en not_active Expired
- 1965-06-15 SE SE785765A patent/SE342447B/xx unknown
- 1965-06-15 CH CH829165A patent/CH451897A/en unknown
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1209155A1 (en) * | 2000-11-20 | 2002-05-29 | Degussa AG | Process for the preparation of propylene oxide free of coupling products |
CN110483445A (en) * | 2019-08-28 | 2019-11-22 | 无锡智归科技有限公司 | The dewatering process of cumyl hydroperoxide and isopropylbenzene in a kind of production of propylene oxide device and its production process |
CN110483445B (en) * | 2019-08-28 | 2022-10-21 | 无锡智归科技有限公司 | Epoxypropane production device and dehydration process of cumene hydroperoxide and cumene in production process thereof |
Also Published As
Publication number | Publication date |
---|---|
FR1459795A (en) | 1966-11-25 |
IL23724A (en) | 1969-04-30 |
ES314229A1 (en) | 1965-11-01 |
DK129932B (en) | 1974-12-02 |
NL6507186A (en) | 1965-12-16 |
DK129932C (en) | 1975-06-16 |
BE665177A (en) | 1965-12-09 |
CH451897A (en) | 1968-05-15 |
DE1518996A1 (en) | 1969-09-18 |
LU48808A1 (en) | 1966-12-12 |
SE342447B (en) | 1972-02-07 |
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