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

被引:58
作者
Saber, Meryem [1 ]
Commenge, Jean-Marc [1 ]
Falk, Laurent [1 ]
机构
[1] Nancy Univ, CNRS, LSGC, F-54001 Nancy, France
关键词
Microchannel; Multi-scale networks; Numbering-up; Flow distribution; Pressure drop; PLATE HEAT-EXCHANGERS; PRESSURE-DROP; CONSTRUCTAL-THEORY; MICROCHANNEL NETS; INTENSIFICATION; OPTIMIZATION; ARRANGEMENT; REACTOR;
D O I
10.1016/j.cep.2008.09.001
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
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. (c) 2008 Elsevier B.V. All rights reserved.
引用
收藏
页码:723 / 733
页数:11
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