(59e) Comprehensive Kinetic Model for Fischer-Tropsch Synthesis Over a Re-Promoted Co/Al2O3 Catalyst | AIChE

(59e) Comprehensive Kinetic Model for Fischer-Tropsch Synthesis Over a Re-Promoted Co/Al2O3 Catalyst

Authors 

Todic, B. S. - Presenter, Texas A&M University at Qatar
Bhatelia, T. J. - Presenter, Texas A&M University at Qatar
Ma, W. - Presenter, University of Kentucky, Center for Applied Energy Research
Jacobs, G. - Presenter, Center for Applied Energy Research, University of Kentucky
Davis, B. H. - Presenter, University of Kentucky, Center for Applied Energy Research
Bukur, D. B. - Presenter, Texas A&M University at Qatar


Abstract

In spite of considerable
effort to develop comprehensive kinetic models for Fischer-Tropsch synthesis
(FTS), there is still a debate about the reaction mechanism and possible
reasons for deviations from Anderson-Schulz-Flory (ASF) distribution. The goal
of this work is to develop a comprehensive kinetic model for FTS on promoted
cobalt-alumina catalyst and provide an insight into this topic.

Experiments were conducted
over 25% Co/0.48%Re/Al2O3 catalyst in 1L stirred tank
slurry reactor over a range of operating conditions (i.e. temperature 220 °C, pressures 200 and 350 psig, H2/CO feed ratio 1.4 and 2.1 and gas space velocity
from 3.6 to 15 NL/g-cat/h). Rate equations were derived on the basis of
Langmuir-Hinshelwood-Hougen-Watson approach using well known carbide mechanism
for FTS [1]. In order to explain non-ASF behavior it was assumed
that the desorption rate of an olefin precursor is a function of carbon number [2].

Kinetic parameters were estimated
by minimizing multiple response objective function using Genetic algorithm and
Levenberg-Marquardt method, as a global and local optimization tool,
respectively. Model evaluation was based on physical meaningfulness of
estimated parameters as well as on statistical relevance of the fit.

Model
yielded physically meaningful values of parameters. Furthermore, it can be seen
from Figure 1 (a-c) that it was also able to correctly predict deviations from
the ASF distribution and olefin to paraffin ratio dependence on carbon number.

Figure 1 ? Comparison of experimental data and model
predictions for C1-15 hydrocarbons at T=220 °C, P=203.3 psig, H2/CO=2.1,
SV=8.0 NL/g-cat/h (a) rates of formation for n-paraffin and 1-olefin; (b) O/P
ratios (1-olefin/n-paraffin); (c) ASF plot (total rates vs. carbon number)

References

[1] LOX E. S., FROMENT G. F. (1993) Kinetics of
the Fischer-Tropsch Reaction on a Precipitated Promoted Iron Catalyst. 2.
Kinetic Modeling. Ind. Eng. Chem. Res. 32, 71-82.

[2] BOTES G. F. (2007) Proposal of a New
Product Characterization Model for the Iron-Based Low-Temperature Fischer-Tropsch
Synthesis. Energy & Fuels, 21, 1379-1389.

 

Acknowledgement

This paper was made possible by NPRP grant 08-173-2-050
from the Qatar National Research Fund (a member of Qatar Foundation). The
statements made herein are solely the responsibility of the authors.

*Corresponding author: Dragomir Bukur,
dragomir.bukur@qatar.tamu.edu