(192a) Interactions Between Flow and Reaction in Catalyst Particles for Hydrogen Generation by Steam Reforming Conference: AIChE Annual MeetingYear: 2009Proceeding: 2009 AIChE Annual MeetingGroup: Catalysis and Reaction Engineering DivisionSession: Catalytic Hydrogen Generation - General I Time: Tuesday, November 10, 2009 - 8:30am-8:51am Authors: Troupel, A., Worcester Polytechnic Institute Taskin, M. E., Worcester Polytechnic Institute Stitt, H., Johnson Matthey Interactions between reaction rates, conduction and diffusion inside catalyst particles can be complex, especially when influenced by non-uniform surface conditions produced by the flow field external to the particle, or by the highly-directional temperature field near a heated tube wall. These non-uniform fields can produce strongly locally-varying rates of reaction, heat transfer and carbon deposition, resulting in local deactivation of the catalyst, over-heating and tube failure. In this work a three-dimensional, realistic flow field is coupled to species and energy simulations in catalyst particles for the highly endothermic methane steam reforming reaction. The simulation domain was a 120-degree segment of a packed tube of tube-to-particle diameter ratio (N) = 4, packed with cylinders. The simulations employed computational fluid dynamics (CFD) and user-defined-codes, to examine packings consisting of full cylinders, hollow cylinders and multi-hole cylinders. The detailed pellet surface and intra-particle temperature, species and reaction rate distributions were obtained for the near-wall particle, along the particle radius and axis. Non-uniform and non-symmetric surface and intra-particle variations were observed, contrary to the conventional modeling approaches, which may lead to mis-evaluation of the intra-particle reaction rates by traditional approaches. Close examination of the flow fields and the particle surface species distributions, along with the temperature distributions in the particles, suggest that these effects are primarily due to the strong temperature gradients at the tube wall, as well as depletion of the reactants in regions of low or stagnant flow where particles approach each other closely.