Abstract
Silica-supported iron catalysts (Fe/SiO2, FePt/SiO2, and FePtK/SiO2) were prepared using a novel nonaqueous (acetone) evaporative deposition technique. This preparation leads to relatively well-dispersed iron phases at modest (10%) metal loadings. Moreover, catalytic activities of these catalysts for Fischer–Tropsch synthesis are high and comparable to industrially relevant precipitated iron catalysts. Catalyst activities were tested following a nonregular L18 orthogonal array that enabled the number of 150-h activity tests to be reduced from 54 to 18; this statistical design was augmented with five additional runs to provide replication. Primary independent variables affecting catalysts' activity were promoter type, pretreatment gas composition (H2, H2/CO, or CO), pretreatment temperature (250, 280, or 320 °C), and reaction temperature (250 or 265 °C); iron carbide level measured from Mössbauer spectroscopy was correlated with activity in a separate analysis. Activity was found to increase in the order Fe/SiO2, FePt/SiO2, and FePtK/SiO2. For a given catalyst composition, activity increases to a maximum with increasing pretreatment temperature and increasing time. Catalyst activity was also positively correlated with increasing chi-carbide content for Fe/SiO2 and FePt/SiO2 catalysts but not for FePtK/SiO2. While pretreatment atmosphere greatly influences initial activity–time behavior, activity is less dependent on pretreatment after about 150 h of reaction. Steady-state methane and C2+ hydrocarbon selectivities (CO2-free basis) for the FePtK/SiO2 catalyst at 250–265 °C, 10 atm, and H2/CO = 1 are 7–9 and 91–93%, respectively, while its hydrocarbon productivity at 250 °C (normalized to 15 atm, H2/CO = 0.7) of 0.27 g HC/gcat/h is comparable to those reported for unsupported precipitated iron catalysts of high activity and selectivity. These results indicate that preparation of an active, selective, stable, attrition-resistant supported iron catalyst for Fischer–Tropsch synthesis is feasible. Promise for additional improvements in catalyst performance through application of advanced preparation methods and optimization of catalyst chemical and physical properties is also indicated.
Similar content being viewed by others
References
F. Fischer and H. Tropsch, Brennstoff-Chem. 7 (1926) 97.
H.H. Storch, N. Golumbic and R.B. Anderson, The Fischer-Tropsch and Related Synthesis. (John Wiley & Sons, New York, 1951).
M.E. Dry, in Part A, The Fischer-Tropsch Synthesis, J.R. Anderson and M. Boudart (eds) (Springer-Verlag, 1981) pp. 159-255.
R.B. Anderson, The Fischer-Tropsch Synthesis (Wiley, New York, 1984).
S. Li, A. Li, S. Krishnamoorthy and E. Iglesia, Catal. Lett. 77 (2001) 197.
P.H. Emmett and S. Brunauer, J. Am. Chem., Soc. 59 (1937) 310.
M.E. Dry, T. Shingles and C.S. van H. Botha, J. Catal. 17 (1970) 341.
H. Arakawa and A.T. Bel, Ind. End. Chem. Process Des. Dev. 22 (1983) 97.
J.L. Rankin and C.H. Bartholomew, J. Catal. 100 (1985) 533.
S.A. Eliason and C.H. Bartholomew, Appl. Catal., A: Gen. 186 (1999) 229.
S. Li, G.D. Meitzner and E. Iglesia, J. Phys. Chem. B 105 (2001) 5743.
D.J. Dwyer and G.A. Somorjai, J. Catal. 52 (1978) 291.
S. Li, S. Krishnamoorthy, A. Li, G.D. Meitzner and E. Iglesia, J. Catal. 206 (2002) 202.
D.B. Bukur and X. Lang, Ind. Eng. Chem. Res. 38 (1999) 3270.
D.S. Kalakkad, M.D. Shroff, S. Kohler, N. Jackson and A.K. Datye, Appl. Catal., A: Gen. 133 (1995) 335.
R. Srinivasan, L. Xu, R.L. Spicer, F.L. Tungate and B.H. Davis, Fuel Sci. & Technol. Int. 14 (1996) 1337.
H.N. Pham, J. Reardon, and A.K. Datye, Powder Technol. 103 (1999) 95.
H.N. Pham, J. Reardon, and A.K. Datye, Powder Technol. 103 (1999) 95.
B.L. Bhatt, E.S. Schoub, E.C. Hedorn, D.M. Herron, D.W. Studer and D.M. Brown, Proc. of the Liquefaction Contractors Review Conf. (Pittsburgh, PA, 1992).
H.N. Pham and A.K. Datye, Symposium on Syngas Conversion to Fuels and Chemicals; 217th National Meeting, (American Chemical Society, Anaheim CA, 1999).
R. Zhang, J.G. Goodwin, Jr. and R. Oukaci, Appl. Catal. 189 (1999) 99.
M.A. Vannice, J. Catal. 37 (1975) 449.
M.A. Vannice, J. Catal. 37 (1975) 462.
G.B. McVicker and M.A. Vannice, J. Catal. 63 (1980) 25.
J.A. Amelse, L.H. Schwartz and J.B. Butt, J. Catal. 72 (1981) 95.
H.J. Jung, J. Catal. 76 (1982) 416.
J.W. Niemantsverdriet, A.M. van der Kraan, W.N. Delgass and M.A. Vannice, J. Phys. Chem. 89 (1985) 67.
V.K. Jones, L.R. Neubauer and C.H. Bartholomew, J. Phys. Chem. 90 (1986) 4832.
J.L. Rankin and C.H. Bartholomew, J. Catal. 100 (1985) 526.
M. Rameswaran and C.H. Bartholomew, J. Catal. 117 (1989) 218.
M.V. Cagnoli, S.G. Marchetti, N.G. Gallegos, A.M. Alvarez, R.C. Mercader and A.A. Yeramian, J. Catal. 123 (1990) 21.
R.J. O'Brien, L. Xu, S. Bao, A.P. Raje and B.H. Davis, Appl. Catal., A: Gen. 196 (2000) 173.
D.B. Bukur and C. Sivaraj, Appl. Catal., A: Gen. 231 (2002) 201.
R.J. Farrauto and C.H. Bartholomew, Fundamentals of Industrial Catalytic Processes. 1st ed. (Blackie Academic and Professional, 1997).
G.W. Huber and C.H. Bartholomew, Stud. Surf. Sci. Catal. 136 (2001) 283.
A. Brenner and D.A. Hucul, Inorg. Chem. 18 (1979) 2836.
E. Iglesia, Appl. Catal., A: Gen. 161 (1997) 59.
C.H. Bartholomew, National Spring Meeting of the AIChE, New Orleans, 2003.
V.I. Kovalchuk and B.N. Kuznetsov, J. Mol. Catal., A: Chem. 102 (1995) 103.
R.D. Jones and C.H. Bartholomew, Appl. Catal. 39 (1988) 77.
J. Xu and C.H. Bartholomew,paper in preparation (2003).
C.F.J. Wu and M. Hamada, Experiments: Planning Analysis and Parameter Design Optimization, 2000.
A. Brenner and J.R.L. Burwell, J. Catal. 52 (1978) 353.
C.H. Bartholomew and M. Boudart, J. Catal. 25 (1972) 173.
J.C.W. Kuo, Final Report Prepared for DOE, Mobil Research and Development Corp., 1985.
H. KÖbel, P. Ackerman and F. Engelhardt, Proc. of the 4th World Petroleum Congress, Section IV/C (Carlo Columbo Publishers, Rome, 1955).
A.P. Raje and B.H. Davis, Catal. Today 36 (1997) 335.
A.P. Raje, R.J. O'Brien, and B.H. Davis, J. Catal. 180 (1998) 36.
R.J. O'Brien, L. Xu, R.L. Spicer and B.H. Davis, Energy and Fuels 10 (1996) 921.
C.H. Bartholomew, L.R. Neubauer and P.A. Smith. Proc. of the 10th International Congress on Catalysis. Budapest (Elsevier Science Publishers, Hungary, 1992).
C.H. Bartholomew, Surface Composition and Chemistry of Carbon Supported Pt-Fe Alloys, Ph.D. Dissertation, (Stanford University, Stanford, 1972.)
B.G. Johnson, C.H. Bartholomew and D.W. Goodman, J. Catal. 128 (1991) 231.
J.A. Rodriguez and D.W. Goodman, Surf. Sci. Rep. 14 (1991) 1.
K.P.R.M. Rao, F.E. Huggins, G.P. Huffman, R.J. Gormley, R.J. O'Brien and B.H. Davis, Energy & Fuels 10 (1996) 546.
S. Sun, C.B. Murray, D. Weller, L. Folks and A. Moser, Science 2000, 1989.
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Xu, J., Bartholomew, C.H., Sudweeks, J. et al. Design, Synthesis, and Catalytic Properties of Silica-Supported, Pt-Promoted Iron Fischer–Tropsch Catalysts. Topics in Catalysis 26, 55–71 (2003). https://doi.org/10.1023/B:TOCA.0000012987.76556.63
Issue Date:
DOI: https://doi.org/10.1023/B:TOCA.0000012987.76556.63