Rl. Keiski et al., STATIONARY AND TRANSIENT KINETICS OF THE HIGH-TEMPERATURE WATER-GAS SHIFT REACTION, Applied catalysis. A, General, 137(2), 1996, pp. 349-370
The high temperature water-gas shift reaction over an industrial Fe3O4
-Cr2O3 catalyst was investigated by stationary and transient experimen
ts in isothermal conditions and at elevated pressures, A new modular c
omputer controlled catalyst evaluation unit which can be operated eith
er as a plug flow tubular reactor (PFTR) or a gradientless reactor was
used. The plug flow mode was used to produce kinetic data for power-l
aw kinetic models and the gradientless reactor to generate kinetic dat
a for classical kinetic models. Separate chemisorption of CO, CO2, and
H-2 were done at 293, 373, 473 and 623 or 673 K to study the importan
ce of these components as surface intermediates in the shift reaction.
In PFTR the kinetic experiments were performed at 3-5 bar and 573-633
K in two separate series during the slow decay of the catalyst activi
ty. The age of the catalyst in these experimental series was 200-280 a
nd 725-763 h, respectively. The transient experiments were performed i
n the gradientless reactor at 573-623 K and 5 bar the age of the catal
yst being 200-870 h. According to the stationary studies, the reaction
rate is strongly dependent on the CO concentration, weakly dependent
on the H2O concentration and practically independent on the CO2 and H-
2 concentrations. The reaction orders with respect to CO and H2O were
around 1 and 0.5. In transient experiments CO2 was always liberated fa
ster than H-2 when the catalyst pretreatment was done without water. D
uring the pretreatment of the catalyst with H2O/N-2, small amounts of
H-2 were formed. The H2O pretreatment retarded the CO2 response. Based
on these results a reaction mechanism was proposed which consisted of
CO adsorption and oxidation steps as well as of H2O adsorption, decom
position and H-2 formation steps. The rate determining steps were the
CO oxidation and H-2 formation steps. Non-dissociative (CO, CO2) and d
issociative (H-2) adsorption were described with Langmuir isotherms.