The influence of the porous support on hydrogen permeation of a Pd-composite membrane in presence of sweep gas has been evaluated. A 20 mu m thick palladium membrane has been prepared by electroless plating on a tubular stainless steel support. H-2 permeation tests have been performed in a laboratory pilot loop up to 400 degrees C and 800 kPa; a nitrogen sweep gas in the 0-100 Nl/h flow rate range has been fed to the permeate side. H-2 flux through the Pd-membrane has been first measured in absence of sweep gas. Permeation can be described by the Sieverts' law and the best fitting of the pressure exponent (n-value) at 400 degrees C is 0.67. Support resistance, estimated by using dusty-gas model equation, determines an increase of H-2 pressure at the interface between Pd-layer and support from 100 to 140 kPa, and a H-2 flux reduction of the 9.8%, approximately. While feeding N-2 as a sweep gas, a H-2 flux much lower than expected by considering Sieverts' law is measured. The difference between experimental results and expected values, calculated by a simple uni-dimensional model is about the 30%, at the higher flow rates. Moreover the increase of n-value from 0.68 up to 0.9 suggests a strong increase in the mass transfer resistance of the support. The resistance to H-2 diffusion due to presence of stagnant N-2 in the support pores has been then estimated by using the dusty gas model equation, which combines Knudsen diffusion, viscous flow and binary diffusion. Results indicate that binary diffusion of H-2 in stagnant N-2 can be responsible of the observed H-2 flux reduction. H-2 partial pressure calculated at the interface between Pd-layer and support in presence of sweep gas is always significantly higher than H-2 partial pressure measured in the permeate. This difference is progressively increasing while increasing sweep gas flow rate and tends to saturate at high flow rates. (c) 2012 Elsevier B.V. All rights reserved.