GB801734A - Carbonylation synthesis reaction - Google Patents
Carbonylation synthesis reactionInfo
- Publication number
- GB801734A GB801734A GB39286/56A GB3928656A GB801734A GB 801734 A GB801734 A GB 801734A GB 39286/56 A GB39286/56 A GB 39286/56A GB 3928656 A GB3928656 A GB 3928656A GB 801734 A GB801734 A GB 801734A
- Authority
- GB
- United Kingdom
- Prior art keywords
- rhodium
- catalyst
- olefins
- aldehyde
- sesquioxide
- 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
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
- C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Oxygenated compounds are prepared by reacting an olefin with carbon monoxide and hydrogen at 60-240 DEG C. and 1000-10,000 p.s.i.g. in the presence of a rhodium-containing catalyst capable of being dissolved in the reaction mixture under the reaction conditions. The rhodium catalyst may be combined with a cobalt catalyst. The olefins may be pure or as hydrocarbon mixtures containing olefins. Specified olefins are non-conjugated diolefins such as dicyclopentadiene and its alkyl derivatives, terpenes and vinylcyclohexene; mono-olefins, cyclic olefins such as cyclohexene; styrene and olefin polymers. In general, C2-20 monomeric olefins and their polymers may be used. The H2:CO ratio is generally 0.5:1 to 10:1, low ratios (0.5-1.5) being preferred for aldehyde production and higher ratios (2-4) for alcohol production. Forms in which the rhodium may be added include metallic rhodium, a rhodium oxide, a salt such as a halide, nitrate, sulfate, sulphite, oleate or stearate or a rhodium carbonyl. A preformed soluble catalyst may be used dissolved in an organic solvent. The catalyst may be deposited on a carrier, generally 1-40 per cent by weight based on rhodium of rhodium compound to the carrier. The catalyst concentration may be from about 0.002 to 20 mol. per cent based on the rhodium to the olefin. The rhodium may be recovered from the product by treatment with water at elevated temperature, e.g. 5-40 per cent by volume water at 80-200 DEG C. In examples: (1) butene-1 is carbonylated to mainly aldehyde products with some acetals and alcohol, reduced rhodium metal/alumina, rhodium sesquioxide and rhodium chloride being mentioned as catalysts; (2) a soluble catalyst is preformed in hexane solution from rhodium sesquioxide and CO/H2 mixture and used for the carbonylation of butene-1; (3) butene-1 is carbonylated using rhodium sesquioxide and the rhodium is recovered from the product by heating with water at 180 DEG C., filtering and drying, and reused; (4) butene-1 is carbonylated using rhodium sesquioxide and the product hydrogenated to amyl alcohols using a nickel catalyst; (5) dicyclopentadiene and alkyl derivatives thereof are carbonylated to the mono-unsaturated aldehyde together with some of the corresponding alcohol using rhodium sesquioxide in hexane solution; the aldehyde may be converted to the acetal and this oxonated further to the aldehyde derivative, which may be hydrolysed to the dialdehyde and subsequently reduced to a glycol; the mono-unsaturated aldehyde may also be reduced to the unsaturated alcohol with metal hydrides and this oxonated further to form, after reduction, a glycol of dicyclopentadiene.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US801734XA | 1956-01-11 | 1956-01-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB801734A true GB801734A (en) | 1958-09-17 |
Family
ID=22155722
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB39286/56A Expired GB801734A (en) | 1956-01-11 | 1956-12-27 | Carbonylation synthesis reaction |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB801734A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3544635A (en) * | 1968-04-15 | 1970-12-01 | Ethyl Corp | Process for preparing alcohols and aldehydes |
DE1618384B1 (en) * | 1967-03-10 | 1971-09-16 | Ruhrchemie Ag | Process for the preparation of tricyclodecane-dimethylols by hydroformylation of dicyclopentadiene over rhodium-containing catalysts and subsequent hydrogenation to give the corresponding diols |
US3989759A (en) * | 1970-07-01 | 1976-11-02 | Atlantic Richfield Company | Hydroformylation process over catalyst having silica alumina support with separate alumina phase and noble metal and cobalt or nickel |
FR2460911A1 (en) * | 1979-07-13 | 1981-01-30 | Ruhrchemie Ag | PROCESS FOR THE PREPARATION OF 3- (4) -FORMYL-TRICYCLO- (5,2,1,0,6) -DECENE-8 |
DE102009001230A1 (en) | 2009-02-27 | 2010-09-02 | Evonik Oxeno Gmbh | Process for the separation and partial recycling of transition metals or their catalytically active complex compounds from process streams |
CN117443456A (en) * | 2023-12-21 | 2024-01-26 | 北京高新利华科技股份有限公司 | Rhodium-phosphine catalyst and preparation method and application thereof |
-
1956
- 1956-12-27 GB GB39286/56A patent/GB801734A/en not_active Expired
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1618384B1 (en) * | 1967-03-10 | 1971-09-16 | Ruhrchemie Ag | Process for the preparation of tricyclodecane-dimethylols by hydroformylation of dicyclopentadiene over rhodium-containing catalysts and subsequent hydrogenation to give the corresponding diols |
US3544635A (en) * | 1968-04-15 | 1970-12-01 | Ethyl Corp | Process for preparing alcohols and aldehydes |
US3989759A (en) * | 1970-07-01 | 1976-11-02 | Atlantic Richfield Company | Hydroformylation process over catalyst having silica alumina support with separate alumina phase and noble metal and cobalt or nickel |
FR2460911A1 (en) * | 1979-07-13 | 1981-01-30 | Ruhrchemie Ag | PROCESS FOR THE PREPARATION OF 3- (4) -FORMYL-TRICYCLO- (5,2,1,0,6) -DECENE-8 |
US4289913A (en) * | 1979-07-13 | 1981-09-15 | Bayer Aktiengesellschaft | Process for preparing 3-(4)-formyltricyclo-[5,2,1,02,6 ]-decene-8 |
DE102009001230A1 (en) | 2009-02-27 | 2010-09-02 | Evonik Oxeno Gmbh | Process for the separation and partial recycling of transition metals or their catalytically active complex compounds from process streams |
WO2010097428A1 (en) | 2009-02-27 | 2010-09-02 | Evonik Oxeno Gmbh | Method for separation and partial return of rhodium and catalytically effective complex compounds thereof from process streams |
CN117443456A (en) * | 2023-12-21 | 2024-01-26 | 北京高新利华科技股份有限公司 | Rhodium-phosphine catalyst and preparation method and application thereof |
CN117443456B (en) * | 2023-12-21 | 2024-04-05 | 北京高新利华科技股份有限公司 | Rhodium-phosphine catalyst and preparation method and application thereof |
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