Supported ferric sulfate and cobalt sulfate catalysts for the oligomerization of olefins
AssigneeConoco Inc.
InventorsRobin M. Dowling, David P. Higley
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Abstract
Iron sulfate supported on alumina or silica alumina and cobalt sulfate supported on alumina are catalysts used for olefin oligomerization. These new catalysts allow olefin oligomerizations to be carried out at lower temperatures than many other known catalysts. The reaction is normally carried out under sufficient pressure to keep the olefin present as a liquid. In addition, the catalysts provide excellent selectivity for the formation of lower olefins and require no water to maintain activity, thereby leading to increased productivity by avoiding problems of polymerization, coking and reactor plugging.
Claims12
A process for the oligomerization of olefins which comprises:
- contacting lightly branched and/or linear olefins in the range of C.sub.2 to C.sub.40 at temperatures in the range of -10.degree. C. to 400.degree. C., and under pressures between 1 and 75 atmospheres, with a catalyst prepared by combining a ferric sulfate solution of a minimum 0.05 molar strength and alumina or silica-alumina support, permitting the support to adsorb the ferric sulfate for a period between 15 minutes to 24 hours so that the weight percent of iron on the support is between 0.005 to 50%, recovering the solid catalyst, drying and calcining the recovered catalyst for a period of from 1 to 12 hours and at a temperature in the range of 250.degree. C. to 700.degree. C.;
- collecting the oligomerized olefinic product.
A process for the oligomerization of olefins which comprises:
- contacting lightly branched and/or linear olefins in the range of C.sub.2 to C.sub.40 at temperatures in the range of -10.degree. C. to 400.degree. C., and under pressures between 1 and 75 atmospheres, with a catalyst prepared by, combining a cobalt sulfate solution of a minimum 0.05 molar strength and alumina support,
- permitting the support to adsorb the cobalt sulfate for a period between 15 minutes to 24 hours so that the weight percent of cobalt on the support is between 0.005% to 50%, recovering the solid catalyst, drying and calcining the recovered catalyst for a period of from 1 to 12 hours and at a temperature in the range of 250.degree. C. to 700.degree. C.,
- collecting the oligomerized olefinic product.
Dependencies are inferred from the claim text.