Cobalt-based catalyst for fischer-tropsch synthesis

Chemistry: fischer-tropsch processes; or purification or recover – Group viii metal containing catalyst utilized for the...

Reexamination Certificate

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C502S242000, C502S243000, C502S244000, C502S245000, C502S251000, C502S252000, C502S253000, C502S258000, C502S259000, C502S260000, C502S261000, C502S263000, C502S305000, C502S326000, C502S327000, C502S328000, C502S329000, C502S330000, C502S331000, C502S332000, C502S335000, C502S336000, C502S337000, C502S338000, C502S340000, C502S341000, C502S342000, C502S343000, C502S344000, C502S345000, C502S346000, C502S352000, C502S355000, C502S407000, C502S415000, C502S439000, C502S524000

Reexamination Certificate

active

08071655

ABSTRACT:
A catalyst applicable to the synthesis gas conversions especially E-T slurry processes, said catalyst comprising: a) a support containing at least a first aluminate element of mixed spinel structure of formula MxM′(1−x)Al2O4/Al2O3.SiO2, x ranging between and excluding 0 and 1, or of simple spinel structure of formula MAl2O4/Al2O3.SiO2, said support being calcined in an at least partly oxidizing atmosphere, at a temperature ranging between 850° C. and 900° C., and b) an active phase deposited on said support, which contains one or more group VIII metals, selected from among cobalt, nickel, ruthenium or iron. Said catalyst is used in a fixed bed or suspended in a three-phase reactor for hydrocarbon synthesis from a CO, H2mixture.

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