出版日期：2000-06-01 00:00:00

著者：Yeh, Ho-ming; Cheng, Tung-wen; Chen, Y. J.

單位：淡江大學化學工程與材料工程學系

出版者：The Society of Chemical Engineers, Japan

著錄名稱、卷期、頁數：Journal of chemical engineering of Japan 33(3), pp.440-448

摘要：This study deals with the effect of an exponential-decay flux of ultrafiltration on the mass transfer rate of solute for dialysis in cross-flow membrane modules. The numerical method of orthogonal collocation was used to solve this problem. The calculated results of solute concentrations and separation efficiencies were analyzed under various operating conditions and decay coefficients of flux in ultrafiltration. The mass transfer rate is usually enhanced by the addition of the effect of ultrafiltration, but this effect decreases as the decay coefficient increases. A significant influence of the decay coefficient on the mass transfer rate appears when the solute transport is dominated by the effect of ultrafiltration, i.e. the conditions of lower dialysate flow rate, lower solute sieving coefficient, or lower overall mass transfer coefficient.

關鍵字：Dialysis;Ultrafiltration;Cross Flow;Membrane Separation

語言：en

ISSN：0021-9592

期刊性質：國外

收錄於：SCI

國別：JPN

出版型式：紙本