The use of intermittent gas bubbling to control membrane fouling in concentrating TCM extract by membrane distillation

被引:56
作者
Ding, Zhongwei [1 ]
Liu, Liying [1 ]
Liu, Zhe [1 ]
Ma, Runyu [1 ]
机构
[1] Beijing Univ Chem Technol, Coll Chem Engn, Beijing 100029, Peoples R China
关键词
Direct contact membrane distillation; Membrane fouling; Gas bubbling; SLUG FLOW; TRANSPORT RESISTANCES; ULTRAFILTRATION FLUX; OSMOTIC EVAPORATION; JUICE CONCENTRATION; HOLLOW FIBERS; MASS-TRANSFER; ORANGE JUICE; WASTE-WATER; CONTACT;
D O I
10.1016/j.memsci.2011.01.063
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study investigates the growth of fouling resistance and fouling limitation through gas bubbling in concentrating the extract of traditional Chinese medicine (TCM) by direct contact membrane distillation (DCMD). Expressions describing the growth rate of fouling resistance and flux decline in concentrating TCM extract by DCMD were deduced. The predicted flux decline by these expressions accords with obtained experimental results, implying that the growth of fouling layer follows the proposed mechanism. To limit membrane fouling or flux decline during concentrating process, intermittent gas bubbling was introduced to the feed side of membrane module. It was confirmed by experimental results that membrane fouling was effectively controlled in the way of removing deposited foulants from membrane surface by created two phase flow. It was also found that the cleaning efficiency of gas bubbling could be improved with the increase of gas flow rate, gas bubbling duration, and the decrease of membrane distillation (MD) duration. These factors combined to affect the cleaning efficiency, and the process productivity may be maximized by the optimization of these gas bubbling conditions. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:172 / 181
页数:10
相关论文
共 39 条
[1]   Concentration of sucrose solutions via vacuum membrane distillation [J].
Al-Asheh, S. ;
Banat, F. ;
Qtaishat, M. ;
Al-Khateeb, M. .
DESALINATION, 2006, 195 (1-3) :60-68
[2]   Orange juice concentration by osmotic evaporation and membrane distillation: A comparative study [J].
Alves, VD ;
Coelhoso, IM .
JOURNAL OF FOOD ENGINEERING, 2006, 74 (01) :125-133
[3]   How slug flow can improve ultrafiltration flux in organic hollow fibres [J].
Cabassud, C ;
Laborie, S ;
Laine, JM .
JOURNAL OF MEMBRANE SCIENCE, 1997, 128 (01) :93-101
[4]   Using direct contact membrane distillation for whey protein concentration [J].
Christensen, Knud ;
Andresen, Rene ;
Tandskov, Iben ;
Norddahl, Birgir ;
du Preez, Jan Heinz .
DESALINATION, 2006, 200 (1-3) :523-525
[5]   The use of gas bubbling to enhance membrane processes [J].
Cui, ZF ;
Chang, S ;
Fane, AG .
JOURNAL OF MEMBRANE SCIENCE, 2003, 221 (1-2) :1-35
[6]   GAS-LIQUID 2-PHASE CROSS-FLOW ULTRAFILTRATION OF BSA AND DEXTRAN SOLUTIONS [J].
CUI, ZF ;
WRIGHT, KIT .
JOURNAL OF MEMBRANE SCIENCE, 1994, 90 (1-2) :183-189
[7]   Effect of the shear intensity on fouling in submerged membrane bioreactor for wastewater treatment [J].
Delgado, S. ;
Villarroel, R. ;
Gonzalez, E. .
JOURNAL OF MEMBRANE SCIENCE, 2008, 311 (1-2) :173-181
[8]   Concentrating the extract of traditional Chinese medicine by direct contact membrane distillation [J].
Ding, Zhongwei ;
Liu, Liying ;
Yu, Hanfei ;
Ma, Runyu ;
Yang, Zurong .
JOURNAL OF MEMBRANE SCIENCE, 2008, 310 (1-2) :539-549
[9]   Fouling resistance in concentrating TCM extract by direct contact membrane distillation [J].
Ding, Zhongwei ;
Liu, Liying ;
Liu, Zhe ;
Ma, Runyu .
JOURNAL OF MEMBRANE SCIENCE, 2010, 362 (1-2) :317-325
[10]   A framework for better understanding membrane distillation separation process [J].
El-Bourawi, M. S. ;
Ding, Z. ;
Ma, R. ;
Khayet, M. .
JOURNAL OF MEMBRANE SCIENCE, 2006, 285 (1-2) :4-29