Effect of operating conditions and potassium content on Fischer-Tropsch liquid products produced by potassium-promoted iron catalysts

The dependencies of Fischer-Tropsch synthesis liquid hydrocarbon product distribution on operating pressure and temperature have been studied over three potassium-promoted iron catalysts with increasing potassium molar content. The study followed an experimental planning and the results were analyze...

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Bibliographic Details
Published inJournal of natural gas chemistry Vol. 17; no. 2; pp. 175 - 178
Main Authors Farias, Francisco E.M., Sales, Fernando G., Fernandes, Fabiano A.N.
Format Journal Article
LanguageEnglish
Published Chengdu Elsevier B.V 01.06.2008
Dalian Institute of Chemical Physics
Universidade Federal do Ceará, Departamento de Engenharia Química, Campus do Pici, Bloco 709, 60455-760 Fortaleza-CE, Brazil
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Summary:The dependencies of Fischer-Tropsch synthesis liquid hydrocarbon product distribution on operating pressure and temperature have been studied over three potassium-promoted iron catalysts with increasing potassium molar content. The study followed an experimental planning and the results were analyzed based on surface response methodology. The effects of different operating conditions and potassium contents on the liquid product distribution were compared based on number average carbon number and dispersion. Results showed that high pressures (25 to 30 arm) favored the production of waxes that could be converted into liquid fuels through hydrocracking, while greater direct selectivity towards diesel was favored by low pressure (20 arm) using catalysts with low potassium to iron molar ratios. The liquid product distribution produced using an iron catalyst with high potassium content presented higher number-average number of carbons when compared to the distribution obtained using an iron catalyst with low potassium content.
Bibliography:Fischer-Tropsch synthesis; liquid fuels; iron-based catalyst; potassium
Fischer-Tropsch synthesis
liquid fuels
potassium
iron-based catalyst
21-1484/O4
TE626.2
ObjectType-Article-2
SourceType-Scholarly Journals-1
ObjectType-Feature-1
content type line 23
ISSN:1003-9953
DOI:10.1016/S1003-9953(08)60047-X