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Article Dans Une Revue Chemical Engineering and Processing: Process Intensification Année : 2009

Rapid design of channel multi-scale networks with minimum flow maldistribution

Résumé

Performing energy and mass transformation within microstructured reactor or processes at industrial scale requires the arrangement of a large number of microchannels (numbering-up process). Appropriate design for uniform flow distribution is a key feature to ensure optimal performance of these channel networks. The present study performs a hydrodynamic analysis of these multi-scale networks under isothermal and laminar flow conditions. The main objective here is to rapidly select an appropriate numbering-up operation, without requiring a large computational power. Therefore, several network configurations are analyzed and compared on the basis of hydrodynamic criteria of interest, such as the flow distribution and the required pumping power. Under a set of geometrical constraints, an optimal multi-scale network can be derived.

Dates et versions

hal-00508829 , version 1 (06-08-2010)

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Citer

M. Saber, J.M. Commenge, L. Falk. Rapid design of channel multi-scale networks with minimum flow maldistribution. Chemical Engineering and Processing: Process Intensification, 2009, 48 (3), pp.723-733. ⟨10.1016/j.cep.2008.09.001⟩. ⟨hal-00508829⟩

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