(246g) Interaction of Hydrogen with Dilute Transition Metal Atoms Dispersed in Supported Liquid Metal Droplets | AIChE

(246g) Interaction of Hydrogen with Dilute Transition Metal Atoms Dispersed in Supported Liquid Metal Droplets

Authors 

MacIntosh, K. - Presenter, Pennsylvania State University
Messick, F., Pennsylvania State University
Rioux, R., Pennsylvania State University
Supported metal catalysts consisting of small amounts of a catalytically active metal dissolved in a liquid metal matrix (typically Ga) and dispersed in the form of droplets on an inert support material are active for hydrocarbon dehydrogenation. Ga has high temperature H2 solubility and permeability, providing opportunities for the development of Ga-based systems for process intensification of equilibrium-limited reactions. SiO2 supported Pd-Ga catalysts with varying Pd contents (molar ratios of 1:20, 1:40, 1:60 and 1:80) were prepared using a facile ultrasoncation-based procedure. H2 adsorption isotherms revealed a significant H2 uptake for all catalysts at elevated temperatures (150 – 550 °C), with Pd content of the catalysts having minimal impact on the H2 uptake. Thermodynamic analysis (van’t Hoff) demonstrated an endothermic heat consistent with associative H2 absorption, consistent with the increase in absorption with increasing temperature. Transient measurements of absorption suggest a fast surface adsorption followed by slow absorption into the bulk. The kinetics of the catalysts were explored using the probe reaction of H2-D2 scrambling. The rate of HD production was found to be significantly higher with increasing Pd-content, however the activation energy was minimally affected. This suggests higher Pd content leads to an increased number of active sites but has a limited effect on the identity of the active sites, suggestive of single site catalyst behavior. Varying the partial pressures of H2 and D2 revealed the mechanism was consistent with non-competitive adsorption and that there was a significant kinetic isotope effect (KIE), found to be around 1.5 in the case of the catalyst with a 1:20 molar ratio. The results here provide insight into the fundamental interactions of H2 with these unique liquid metal catalysts, which will aid in the optimization of their performance for H2-based reactions where simultaneous separation is advantageous.