Micro-scale distillation: simulation

被引:5
作者
Fanelli, M.
Arora, R.
Glass, A.
Litt, R.
Qiu, D.
Silva, L.
Tonkovich, A. L.
Weidert, D.
机构
来源
Computational Methods in Multiphase Flow IV | 2007年 / 56卷
关键词
distillation; simulation; separation; vapour-liquid; microchannel;
D O I
10.2495/MPF070201
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Microchannel technology as applied to chemical processing has resulted in impressive improvements in performance thresholds. Studies published for more than a decade show that enhanced performance in chemical reactors can be largely attributed to the reduction of transport distances. Chemical distillation is now emerging as a new area for the application of microchannel technology. A simplified method for simulating a microchannel distillation process has been developed and validated with experimental data. Both simulation and experiments show that the height of a theoretical transfer unit for the separation of hexane and cyclohexane in a microchannel distillation unit is reduced to centimetres. Vapour-side resistance was found to control mass transfer for the cases considered. The current simulation can serve as a tool for optimizing and refining the design of multiphase microchannel processes.
引用
收藏
页码:205 / 213
页数:9
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