Fischer–Tropsch principles of co-hydrogenation on iron catalysts

The temporal changes of product composition together with changes of the catalyst in composition and structure have been investigated for Fischer–Tropsch synthesis with an alkalized precipitated iron catalyst at 250°C, 1 MPa, using a special synthesis gas with a molar H2/CO2-ratio of three. It was observed that the steady state of synthesis developed in processes of self-organization during several episodes with individual kinetic regimes. The“true FT catalyst” apparently was “constructed” at reaction conditions under complete consumption of α-iron and formation of iron carbide (Fe5C2). The magnetite phase disappeared partially and a new “unknown” (probably FeOx) phase was formed. It has been concluded from the data of chain growth and branching probability that during self-organization only the number of sites increased but their nature remained unchanged. Strong spatial constraints appear to apply at the sites.  On iron catalysts, the FT sites are very stable, invariant against changes in reaction conditions, in contrast to FT synthesis on cobalt. There the sites show a dynamic behavior.

[1]  Hans Schulz,et al.  Kinetics of Fischer-Tropsch selectivity , 1988 .

[2]  H. Schulz,et al.  Construction of the Fischer Tropsch regime with cobalt catalysts , 2002 .

[3]  R. Anderson,et al.  The Fischer-Tropsch Synthesis , 1984 .

[4]  Hans Schulz,et al.  Selectivity and mechanism of Fischer-Tropsch synthesis with iron and cobalt catalysts , 1994 .

[5]  Hans Schulz,et al.  Kinetic modelling of Fischer–Tropsch product distributions , 1999 .

[6]  Hans Schulz,et al.  Reactions of α-olefins of different chain length added during Fischer–Tropsch synthesis on a cobalt catalyst in a slurry reactor , 1999 .

[7]  Andre Peter Steynberg,et al.  High temperature Fischer–Tropsch synthesis in commercial practice , 1999 .

[8]  Jon Wilson,et al.  Atomic-Scale Restructuring in High-Pressure Catalysis , 1995 .

[9]  H. Kölbel,et al.  Kohlenwasserstoffe aus Kohlenoxyd und Wasser , 1952 .

[10]  H. Schulz,et al.  Mechanism of the Fischer Tropsch Process , 1988 .

[11]  P. Albers,et al.  Catalyst poisoning by methyl groups , 1999 .

[12]  H. Schulz,et al.  Selectivity of Fischer-Tropsch Synthesis: Spatial constraints and forbidden reactions , 2001 .

[13]  T. Riedel,et al.  Fischer–Tropsch on Iron with H2/CO and H2/CO2 as Synthesis Gases: The Episodes of Formation of the Fischer–Tropsch Regime and Construction of the Catalyst , 2003 .

[14]  H. Schulz,et al.  Effect of water partial pressure on steady state Fischer-Tropsch activity and selectivity of a promoted cobalt catalyst , 1997 .

[15]  H. Storch The Fischer-Tropsch and related syntheses , 1951 .

[16]  H. Schulz Major and Minor Reactions in Fischer–Tropsch Synthesis on Cobalt Catalysts , 2003 .

[17]  E. Iglesia,et al.  Iron catalyzed CO2 hydrogenation to liquid hydrocarbons , 1998 .

[18]  H. Schulz,et al.  Specific inhibition as the kinetic principle of the Fischer-Tropsch synthesis , 1995 .