The kinetic of the direct CO2 hydrogenation to higher hydrocarbons via Fischer-Tropsch synthesis (FTS) and reverse water-gas shift reaction (RWGS) mechanisms over a series of precipitated Fe/Cu/K catalysts with various particle sizes were studied in a well mixed, continuous spinning basket reactor. The iron catalysts promoted with copper and potassium were prepared via precipitation technique in various alcohol/water mixtures to achieve a series of catalyst particle sizes between 38-14 nm. A new kinetic model for direct CO2 hydrogenation was developed with combination of kinetic model for FTS reaction and RWGS equilibrium condition. For estimate of structure sensitivity of indirect CO2 hydrogenation to higher hydrocarbons, the kinetic parameters of developed model are evaluated for a series of iron catalysts with various particle sizes. For kinetic study a wide range of syngas conversions have been obtained by varying experimental conditions. The results show that the new developed model fit favorably with experimental data. The values of activation energies for indirect CO2 hydrogenation reaction are fall within the narrow range of 23–16 kJ/mol.

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