Catalyst – solid sorbent – or support therefor: product or process – Catalyst or precursor therefor – Sulfur or compound containing same
Reexamination Certificate
2003-06-26
2009-02-03
Hailey, Patricia L (Department: 1793)
Catalyst, solid sorbent, or support therefor: product or process
Catalyst or precursor therefor
Sulfur or compound containing same
C502S202000, C502S208000, C502S209000, C502S210000, C502S211000, C502S212000, C502S213000, C502S214000, C502S215000, C502S219000, C502S305000, C502S306000, C502S307000, C502S308000, C502S309000, C502S310000, C502S311000, C502S312000, C502S313000, C502S314000, C502S315000, C502S316000, C502S317000, C502S318000, C502S319000, C502S320000, C502S321000, C502S322000, C502S323000, C502S324000, C502S344000, C502S347000, C502S348000
Reexamination Certificate
active
07485597
ABSTRACT:
A method for improving the selectivity of a supported highly selective epoxidation catalyst comprising silver in a quantity of at most 0.17 g per m2surface area of the support, which method comprisescontacting the catalyst, or a precursor of the catalyst comprising the silver in cationic form, with a feed comprising oxygen at a catalyst temperature above 250° C. for a duration of up to 150 hours, andsubsequently decreasing the catalyst temperature to a value of at most 250° C.; anda process for the epoxidation of an olefin, which process comprisescontacting a supported highly selective epoxidation catalyst comprising silver in a quantity of at most 0.17 g per m2surface area of the support, or a precursor of the catalyst comprising the silver in cationic form, with a feed comprising oxygen at a catalyst temperature above 250° C. for a duration of up to 150 hours, andsubsequently decreasing the catalyst temperature to a value of at most 250° C. and contacting the catalyst with the feed comprising the olefin and oxygen.
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Lockemeyer John Robert
Reinalda Donald
Yeates Randall Clayton
Hailey Patricia L
Shell Oil Company
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