Porous matrices are often used to provide structural support to thin Pd-based metallic membranes in H(2) separation applications. Optimizing such composite membranes requires detailed understanding of all possible rate-controlling processes including surface and bulk processes in the metal and diffusion of gases through the porous media. In the work described in this paper, we fabricate a composite membrane by depositing a thin (similar to 5-6 mu m) Pd film on a porous alpha-Al(2)O(3) tube and then measure the H(2) permeance of this composite membrane over a range of operating conditions. The rate-controlling processes for the H(2) permeation are evaluated with a computational model which combines a detailed thermo-kinetic Pd-H(2) interaction model and a porous media transport model. The Pd-H(2) thermo-kinetic model is validated against literature data, and the porous media transport model is independently calibrated using experimental measurements. The combined composite membrane model gives good agreement with experiments over a large range of temperatures (250-450 degrees C) and H(2) partial pressures (100-385 kPa). This validated model is then used to analyze the importance of design parameters such as Pd thickness and support micro-structure on H(2) flux through the membrane. These parametric studies will also aid in assessing trade-offs between membrane structural robustness and overall performance. (C) 2010 Elsevier B.V. All rights reserved.