Modeling of cross-flow microfiltration of fine particle/macromolecule binary suspension

被引:21
作者
Hwang, KJ [1 ]
Cheng, YH
Tung, KL
机构
[1] Tamkang Univ, Dept Chem & Mat Engn, Taipei 25137, Taiwan
[2] Chung Yuan Christian Univ, Dept Chem Engn, Taoyuan 320, Taiwan
[3] Chung Yuan Christian Univ, R&D Ctr Membrane Technol, Taoyuan 320, Taiwan
关键词
cross-flow microfiltration; binary suspension; cake properties; rejection of macromolecules; membrane separation;
D O I
10.1252/jcej.36.1488
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The cross-flow microfiltration of fine particle/macromolecule binary suspension is analyzed and modeled in this study. The filtration rate, the cake thickness and the rejection of macromolecules can be estimated from the operating variables by modeling the cake formation, the concentration polarization and the penetration of macromolecules through the filter cake. Based on the force balance model, the thickness of the filter cake formed by fine particles can be related to the operating conditions. The formed cake plays the major roles on the filtration resistances and on the rejection of macromolecules. A reversible concentration polarization layer is constructed with the macromolecules near the cake surface. The concentration profile in this layer can be calculated using the mass transfer equation once the mass transfer coefficient is obtained from the analogy analysis. The standard capture equation for depth filtration is adopted to simulate the retention and the penetration of macromolecules in the filter cake. Experiments are carried out using the binary suspensions prepared by polymethyl methacrylate (PMMA) particles and the Dextran macromolecules. The filtration rates, the rejection of Dextran and the cake properties under various operating conditions are measured and discussed. The predicted values using the proposed models agree fairly well with the experimental data under various operating conditions.
引用
收藏
页码:1488 / 1497
页数:10
相关论文
共 18 条
[1]   YEAST CAKE LAYERS AS SECONDARY MEMBRANES IN DEAD-END MICROFILTRATION OF BOVINE SERUM-ALBUMIN [J].
ARORA, N ;
DAVIS, RH .
JOURNAL OF MEMBRANE SCIENCE, 1994, 92 (03) :247-256
[2]   THE BEHAVIOR OF SUSPENSIONS AND MACROMOLECULAR SOLUTIONS IN CROSS-FLOW MICROFILTRATION [J].
BELFORT, G ;
DAVIS, RH ;
ZYDNEY, AL .
JOURNAL OF MEMBRANE SCIENCE, 1994, 96 (1-2) :1-58
[3]   Resistance analyses for ultrafiltration in tubular membrane module [J].
Cheng, TW ;
Yeh, HM ;
Gau, CT .
SEPARATION SCIENCE AND TECHNOLOGY, 1997, 32 (16) :2623-2640
[4]  
Cheryan M., 1998, ULTRAFILTRATION MICR, P113, DOI DOI 10.1201/9781482278743
[5]   GROWTH OF THE POLARIZATION LAYER IN ULTRAFILTRATION WITH HOLLOW-FIBER MEMBRANES [J].
CLIFTON, MJ ;
ABIDINE, N ;
APTEL, P ;
SANCHEZ, V .
JOURNAL OF MEMBRANE SCIENCE, 1984, 21 (03) :233-246
[6]  
Fischer E., 1985, GER CHEM ENG, V8, P211
[7]   Stability of latex crossflow filtration:: cake properties and critical conditions of deposition [J].
Gésan-Guiziou, G ;
Wakeman, RJ ;
Daufin, G .
CHEMICAL ENGINEERING JOURNAL, 2002, 85 (01) :27-34
[8]   Microfiltration of protein mixtures and the effects of yeast on membrane fouling [J].
Güell, C ;
Czekaj, P ;
Davis, RH .
JOURNAL OF MEMBRANE SCIENCE, 1999, 155 (01) :113-122
[9]  
HERMIA J, 1982, T I CHEM ENG-LOND, V60, P183
[10]   The role of dynamic membrane in cross-flow microfiltration of macromolecules [J].
Hwang, KJ ;
Cheng, YH .
SEPARATION SCIENCE AND TECHNOLOGY, 2003, 38 (04) :779-795