Hydroformylation of olefins
AssigneeExxon Research & Engineering Co.
InventorJean A. A. Hanin
Life of this patent
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Abstract
The higher alcohol yield of a hydroformylation process comprising catalytic hydroformylation of olefinic feedstock and hydrogenation of the crude product is improved by separating light materials and desired alcohols from the hydrogenated product, and then subjecting the remaining heavy materials to catalytic steam cracking at 260.degree.-380.degree. C. The fraction of the cracked product which is rich in alcohol/aldehyde is then separated and recycled, preferably to the hydrogenation stage.
Claims14
A process for producing higher alcohols from an olefinic feedstock comprising olefins containing from 6 to 12 carbon atoms which comprise:
- (a) hydroformylating said olefinic feedstock with synthesis gas in the presence of a cobalt-containing hydroformylation catalyst to form a hydroformylation product mixture containing higher aldehydes and higher alcohols having a carbon number which is one carbon atom greater than said olefinic feedstock, unreacted olefinic feedstock and secondary reactions products;
- (b) treating said hydroformylation product mixture to remove said hydroformylation catalyst therefrom and to form a decobalted hydroformylation product mixture;
- (c) hydrogenating said decobalted hydroformylation product mixture to convert said higher aldehydes to additional amounts of said higher alcohols;
- (d) distilling the higher alcohol-containing hydrogenation product mixture formed in step (c) to separate (i) a lower boiling light oxo fraction and (ii) said higher alcohols from (iii) a higher boiling heavy oxo fraction;
- (e) subjecting the heavy oxo fraction to catalytic steam cracking at a temperature of from 260.degree. to 380.degree. C. in the presence of a cracking catalyst selected from the group consisting of active metal oxides and pseudo-metal oxides, to form a cracked heavy oxo fraction mixture comprising a major proportion of higher alcohol and higher aldehyde, and a minor proportion of olefin, saturated hydrocarbon and uncracked heavy oxo fraction residue;
- and (f) recycling said cracked heavy oxo fraction mixture to the hydroformylation or hydrogenation stage of the process.
Dependencies are inferred from the claim text.