GB902368A - Oxidation of alcohols - Google Patents
Oxidation of alcoholsInfo
- Publication number
- GB902368A GB902368A GB32224/59A GB3222459A GB902368A GB 902368 A GB902368 A GB 902368A GB 32224/59 A GB32224/59 A GB 32224/59A GB 3222459 A GB3222459 A GB 3222459A GB 902368 A GB902368 A GB 902368A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- catalyst
- halogen
- added
- manganese
- 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
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/30—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with halogen containing compounds, e.g. hypohalogenation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A catalyst for oxidizing alcohols to carbonyl compounds at a pH below 4 comprises a halogen-containing compound of platinum, palladium, or rhodium. The metal is present or is brought to the higher valency form in which it can exist. The catalyst may be supported and may include an acid compound, e.g. hydrochloric acid, sulphuric acid, phosphoric acid, trifluoroacetic acid, alkyl or aryl sulphonic acids, halogen-substituted alkyl or aryl sulphonic acids or boron fluoride complexes. When a non-halogen acid is added halogens may be added to the catalyst in the form of salts, e.g. ammonium, manganese or cupric chloride. There may also be present compounds or ions of Group I, II, V, VI and VII metals, e.g. copper, silver, mercury, vanadium, chromium or manganese. The catalyst may be regenerated by treatment with oxygen. An activator may be present in the reaction or regeneration zone. Suitable activators are, for example, hydrogen bromide, ozone, t-butyl peroxide, benzoyl peroxide, cumene hydro-peroxide, cumene, iodine, nitric oxide, quinone, aldehydes and isobutyro-azo-dinitrile.ALSO:Carbonyl compounds are produced by intimately contacting a feed comprising a C2 to C8 saturated alcohol in the liquid phase and at a pH below 4 with a catalyst comprising a halogen-containing compound of platinum, palladium or rhodium at a temperature in the range 50-300 DEG C., and recovering a saturated carbonyl compound having the same number of carbon atoms as the alcohol. The metal is present in the higher valency form in which it exists. The alcohol used as feed may be formed in situ from the corresponding olefine. The preferred catalyst is chlorplatinic acid. The catalysts may include an acid compound, e.g. hydrochloric acid, sulphuric acid, phosphoric acid, trifluoroacetic acid, alkyl or aryl sulphonic acid, halogen substituted alkyl or aryl sulphonic acids or boron fluoride complexes. When a non-halogen acid is used halogens may be added in the form of salts, e.g. ammonium, manganese or cupric chloride. There may also be present compounds or ions of Group I, II, V, VI and VII metals e.g. copper, silver, mercury, vanadium, chromium or manganese. The catalyst may be used on a support. An organic solvent, e.g. benzene, toluene, xylene, tetrahydrofuran, biphenyl, chlorobenzene, dichlorobenzene and alcohols such as C8-C20 alcohols or neopentyl alcohol, may be used. If desired, oxygen may be passed into the reaction mixture and the catalyst may be regenerated by treatment with oxygen. Chelating agents or catalyst activators may also be added to the mixture in the reaction zone or activators may be added to the catalyst in the regenerating zone.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US789901A US3080426A (en) | 1959-01-29 | 1959-01-29 | Oxidation of alcohols |
Publications (1)
Publication Number | Publication Date |
---|---|
GB902368A true GB902368A (en) | 1962-08-01 |
Family
ID=25149038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB32224/59A Expired GB902368A (en) | 1959-01-29 | 1959-09-22 | Oxidation of alcohols |
Country Status (2)
Country | Link |
---|---|
US (1) | US3080426A (en) |
GB (1) | GB902368A (en) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3202717A (en) * | 1960-08-04 | 1965-08-24 | Dow Chemical Co | Method of oxidizing mono-olefins |
US3202715A (en) * | 1960-08-04 | 1965-08-24 | Dow Chemical Co | Method of oxidizing mono-olefins |
NL292182A (en) * | 1962-05-02 | 1965-07-12 | ||
BE758517A (en) * | 1970-11-05 | 1971-04-16 | Labofina Sa | SECONDARY ALCOHOLS OXIDATION PROCESS |
US3941811A (en) * | 1971-07-01 | 1976-03-02 | Roussel-Uclaf | Oxidation process |
US4218401A (en) * | 1974-01-11 | 1980-08-19 | The Dow Chemical Company | Oxydehydrogenation of alcohols |
DE2548908C3 (en) * | 1975-10-31 | 1978-04-27 | Bayer Ag, 5090 Leverkusen | Process for the production of formaldehyde |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2690457A (en) * | 1954-09-28 | Process fok the production of un | ||
US1999620A (en) * | 1929-05-23 | 1935-04-30 | Shell Dev | Process for the manufacture of alcohols |
US2010066A (en) * | 1929-08-19 | 1935-08-06 | Dreyfus Henry | Manufacture of aliphatic ketones |
US1978824A (en) * | 1934-04-07 | 1934-10-30 | Commercial Solvents Corp | Production of ketones |
DE713791C (en) * | 1934-07-19 | 1941-11-14 | Bernh Draeger | Conversion of carbon dioxide contained in gas mixtures in small quantities into carbon dioxide by oxidation |
US2354683A (en) * | 1942-05-01 | 1944-08-01 | Eastman Kodak Co | Oxidation of secondary alcohols |
FR891209A (en) * | 1942-10-17 | 1944-03-01 | Process for preparing acetaldehyde for the manufacture of acetic acid, para and metaldehyde, aldol, etc. | |
GB767409A (en) * | 1953-12-23 | 1957-02-06 | Ici Ltd | Improvements in or relating to the production of ketones |
-
1959
- 1959-01-29 US US789901A patent/US3080426A/en not_active Expired - Lifetime
- 1959-09-22 GB GB32224/59A patent/GB902368A/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
US3080426A (en) | 1963-03-05 |
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