Membrane distillation .1. Module design and performance evaluation using vacuum membrane distillation

被引:186
作者
Lawson, KW
Lloyd, DR
机构
[1] Separations Research Program, Department of Chemical Engineering, University of Texas at Austin, Austin
关键词
liquid permeability and separations; membrane distillation; microporous and porous membranes; vacuum MD;
D O I
10.1016/0376-7388(96)00140-8
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pure water vacuum membrane distillation (VMD) experiments were performed to evaluate the heat and mass transfer boundary layer resistances in a new laboratory-scale membrane module. The membrane module designed for this work is unique in that it can use flat-sheet membranes without a support. Additionally, the membrane module and associated apparatus were designed to achieve relatively high feed and permeate Reynolds numbers within the module. These two factors led to a dramatic reduction in boundary layer resistances, which resulted in improved VMD fluxes. This paper also examines a new complete VMD model based on the dusty-gas model, which accounts for both Knudsen and viscous mass transport across the membrane. The new model was used to predict the performance of VMD with pure water and ethanol-water solutions.
引用
收藏
页码:111 / 121
页数:11
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