Constraints determining the selectivity of Fischer-Tropsch synthesis and related process opportunities

PETR 142

Hans Schulz, Hans.Schulz@ciw.uni-karlsruhe.de, Engler-Bunte-Institute, University Krlsruhe, Kaiserstrasse 12, 76128 Karlsruhe, Germany
Fischer Tropsch synthesis is frequently addressed as unselective, because a multi-compound product is obtained. But compared with the composition of petroleum or the oil from coal hydrogenation, the FT-product is very uniform and very clean. Referring to the reaction pathway it can be regarded as very selective: “Only” aliphatic hydrocarbon chains are formed from carbon monoxide and hydrogen. It is discussed how specific constraints rule the unique FT-selectivity: - Frustration of chain desorption (this allowing for chain growth), - frustration of CO-methanation, - low paraffin-to-olefin chain desorption probability, - low branching- to linear chain growth probability.

Options for valuable product compositions are considered, following the rules of the Fischer-Tropsch-regime. It is discussed how the selectivity can be directed to - small linear alpha-olefins, - medium carbon number range alpha-olefins, - motor gasoline, - diesel fuel - and waxes

Modifying the FT-selectivity by applying a second kind of catalyst (e.g. zeolites) under reaction conditions has not yet shown convincing aspects because of undue conditions for the one or the other catalytic system and also deactivation problems. Favorable processes are possible by combination of FT-synthesis with consecutive “ideal” bifunctional hydroisomerization and hydrocracing for diesel fuel, gasoline and lubricants or with mild thermal paraffin cracking to produce olefins of higher carbon number.