Abstract:An experimental study was performed with an aged Co/Pt/Al 2 O 3 catalyst in a laboratory slurry reactor to develop a macrokinetic expression for the Fischer-Tropsch (FT) synthesis. A semiempirical model was found to be the preferred two-parameter rate equation of the reaction. However, it was shown that this model is virtually indistinguishable from a mechanistically derived three-parameter rate model that assumes the following kinetically relevant steps in the cobalt-FT synthesis: CO dissociation occurs witho… Show more
“…Direct comparison of catalyst performance can only be done at exactly the same reactor conditions. As this is cumbersome to achieve experimentally, Fischer-Tropsch synthesis activities were expressed in terms of the dimensionless relative intrinsic activity factor (RIAF), defined as the normalized rate constant (k) of the published [29] kinetic equation:…”
“…Direct comparison of catalyst performance can only be done at exactly the same reactor conditions. As this is cumbersome to achieve experimentally, Fischer-Tropsch synthesis activities were expressed in terms of the dimensionless relative intrinsic activity factor (RIAF), defined as the normalized rate constant (k) of the published [29] kinetic equation:…”
“…performed a macro-kinetic study for cobalt and iron FTS catalysts wherein operating conditions were systematically varied in a wide range [6,7]. They found that equations 1 and 2 show systematic statistical deviations and therefore proposed different equations (equation 3 and 4) for cobalt and iron respectively.…”
“…When mechanistic pathways are not available from fundamental knowledge, empirical studies are done where macro kinetic models are derived [34] for a large set of feasible mechanisms and tested against laboratory data. The best candidate model is then identified using rigorous statistical criteria [35] and a reaction mechanism postulated for further study.…”
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