کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
687520 | 889328 | 2009 | 11 صفحه PDF | دانلود رایگان |

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.
Journal: Chemical Engineering and Processing: Process Intensification - Volume 48, Issue 3, March 2009, Pages 723–733