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- 2011 Annual Meeting
- Fuels and Petrochemicals Division
- Catalytic Biomass Conversion to Chemicals I
- (508f) Kinetics of the Water-Gas Shift Reaction In the Liquid Phase
The liquid phase WGS reaction (LWGS) was carried out on two different catalysts – Pt/C and PtMo/C. The TOR* obtained for PtMo/C (~0.05s-1) was observed to be 10 times higher than that for Pt/C (~0.005s-1). A factor of about 10 was also observed for both gas-phase WGS and the glycerol reforming reaction. The gas-phase WGS TOR was extrapolated to LWGS conditions and vice-versa in order to compare the two. The TOR obtained in LWGS was found to be about 10 times higher than that for the gas-phase WGS. In LWGS on Pt/C, a higher CO order (~0.5) as compared to gas-phase WGS (~0.2) was observed, indicating lower coverage of CO. This can be explained by competitive adsorption between CO and H2O. Carbon dioxide was found to be significantly more inhibiting in LWGS (~-0.3) as compared to gas-phase WGS (~-0.1). We attribute this to a lower temperature of operation as well as the higher partial pressure range of CO2 over which the order was measured. The H2 orders in LWGS and gas-phase WGS are similar (~-0.33). The kinetic data for WGS at liquid phase reforming conditions are the first reported and the results are consistent with predictions made by extrapolation from gas-phase conditions.
*All the TOR values have been normalized to T=160°C, PCO=4bar, PH2=4bar, PCO2=0.2bar, PH2O=4.7bar