FIELD: process engineering.
SUBSTANCE: invention relates to Fisher-Tropsh synthesis catalysts. Fisher-Tropsh catalyst comprise carrier and active cobalt-containing component Note here that said component represents cobalt oxide structures immobilised on catalyst surface that feature maximum hydrogen consumption at 500-800°C on graph of thermally programmed reduction. Note also that amount of cobalt oxide structures on catalyst surface should be sufficient for use of 0.3 mmol of H2/g catalyst. Invention covers also method of producing above describe catalyst comprising adding cobalt on liquid or solid phase carrier to perform catalyst activation to form active cobalt-containing component in the form of immobilised surface cobalt oxide structures. It covers also method of producing hydrocarbons on above described Fisher-Tropsh synthesis catalyst via conversion of CO and H2 at 180 to 300°C and 0.1 to 3 MPa.
EFFECT: highly active and selective Fisher-Tropsh catalyst.
11 cl, 2 tbl, 2 dwg, 10 ex
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Authors
Dates
2011-06-27—Published
2009-08-04—Filed