References
- Annaland, M. V. S., Kuipers, J. A. M., and Swaij, W. P. M. V. 2001. A kinetic rate expression for the time-dependent coke formation rate during propane dehydrogenation over a platinum alumina monolithic catalyst. Catal. Today 66:427–436.
- Aparicio, F. P., Rodriguez-Ramos, I., and Guerrero-Ruiz, A. 2002. On the performance of porous vycor membranes for conversion enhancement in the dehydrogenation of methylcyclohexane to toluene. J. Catal. 212:182–192.
- Balat, M., and Özdemir, N. 2005. New and renewable hydrogen production processes. Energy Sources 27:1285–1298.
- Chaouki, J., and Klvana, D. 1994. Influence of the deactivation of an industrial Pt-Sn/Al2O3 catalyst on the performance of the dehydrogenation reactor. Chem. Eng. Sci. 49:4639–4646.
- Demirbaş, A. 2005. Hydrogen and boron as recent alternative motor fuels. Energy Sources 27:741–748.
- Itoh, N., Tamura, E., Hara, S., Takahashi, T., Shono, A., Satoh, K., and Namba, T. 2003. Hydrogen recovery from cyclohexane as a chemical hydrogen carrier using a palladium membrane reactor. Catal. Today 82:119–125.
- Kariya, N., Fukuoka, A., Utagawa, T., Sakuramoto, M., Goto, Y., and Ichikawa, I. 2003. Efficient hydrogen production using cyclohexane and decalin by pulse-spray mode reactor with Pt catalysts. Appl. Catal. A 247:247–259.
- Lindfors, L. P., and Salmi, T. 1993. Kinetics of toluene hydrogenation on a supported Ni catalyst. Ind. Eng. Chem. Res. 32:34–42.
- Schildhauer, T., Newson, E., and Müller, S. 2001. The equilibrium constant for the methylcyclohexane-toluene system. J. Catal. 198:355–358.