Experimental and theoretical analyses of temperature polarization effect in vacuum membrane distillation

被引：128

作者：

Alsaadi, Ahmad S. ^{[1
]}

Francis, Lijo ^{[1
]}

Amy, Gary L. ^{[1
]}

Ghaffour, Noreddine ^{[1
]}

机构：

[1] KAUST, Water Desalinat & Reuse Ctr, Thuwal 239556900, Saudi Arabia

来源：

JOURNAL OF MEMBRANE SCIENCE | 2014年 / 471卷

关键词：

Vacuum membrane distillation (VMD); Temperature polarization; Mass transfer coefficient; Heat transfer; Flux sensitivity factor; EXTRACTS AQUEOUS-SOLUTION; HOLLOW-FIBER MEMBRANES; PERFORMANCE EVALUATION; SEAWATER DESALINATION; OPERATING-CONDITIONS; REVERSE-OSMOSIS; MASS-TRANSFER; TRANSPORT RESISTANCES; AROMA COMPOUNDS; HEAT-TRANSFER;

D O I：

10.1016/j.memsci.2014.08.005

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

This paper discusses the effect of temperature polarization in Vacuum Membrane Distillation (VMD). The main motivation for using VMD in this work is that this module configuration is much simpler and more suitable for this kind of investigation than the other MD configurations such as Direct Contact Membrane Distillation (DCMD). The coupling between heat and mass transfer mechanisms at the feed-membrane interface is presented from a theoretical point of view. In addition, a new simple graphical method and a mathematical model for determining VMD flux are presented. The two methods used in evaluating the extent of temperature polarization effect on water vapor flux (flux sensitivity factors and temperature polarization coefficient (TPC)) are also analyzed and compared. The effect of integrating a heat recovery system in a large scale module on the TPC coefficient has also been studied and presented in this paper. (C) 2014 Elsevier B.V. All rights reserved.

引用

页码：138 / 148

页数：11

共 61 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] Modelling flow and heat transfer in spacer-filled membrane distillation channels using open source CFD code [J].

Al-Sharif, Sharaf ;

Albeirutty, Mohammed ;

Cipollina, Andrea ;

Micale, Giorgio .

DESALINATION, 2013, 311 :103-112

[3] Experimental and theoretical evaluation of temperature polarization phenomenon in direct contact membrane distillation [J].

Ali, A. ;

Macedonio, F. ;

Drioli, E. ;

Aljlil, S. ;

Alharbi, O. A. .

CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (10) :1966-1977

[4] Modeling of air-gap membrane distillation process: A theoretical and experimental study [J].

Alsaadi, A. S. ;

Ghaffour, N. ;

Li, J. -D. ;

Gray, S. ;

Francis, L. ;

Maab, H. ;

Amy, G. L. .

JOURNAL OF MEMBRANE SCIENCE, 2013, 445 :53-65

[5] Recovery of volatile aroma compounds from black currant juice by vacuum membrane distillation [J].

Bagger-Jorgensen, R ;

Meyer, AS ;

Varming, C ;

Jonsson, G .

JOURNAL OF FOOD ENGINEERING, 2004, 64 (01) :23-31

[6] Recovery of volatile fruit juice aroma compounds by membrane technology: Sweeping gas versus vacuum membrane distillation [J].

Bagger-Jorgensen, Rico ;

Meyer, Anne S. ;

Pinelo, Manuel ;

Varming, Camilla ;

Jonsson, Gunnar .

INNOVATIVE FOOD SCIENCE & EMERGING TECHNOLOGIES, 2011, 12 (03) :388-397

[7] Treatment of waters colored with methylene blue dye by vacuum membrane distillation [J].

Banat, F ;

Al-Asheh, S ;

Qtaishat, M .

DESALINATION, 2005, 174 (01) :87-96

[8] Desalination by vacuum membrane distillation: sensitivity analysis [J].

Banat, F ;

Abu Al-Rub, F ;

Bani-Melhem, K .

SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 33 (01) :75-87

[9] Removal of benzene traces from contaminated water by vacuum membrane distillation [J].

Banat, FA ;

Simandl, J .

CHEMICAL ENGINEERING SCIENCE, 1996, 51 (08) :1257-1265

[10] Heat and mass transport resistances in vacuum membrane distillation per drop [J].

Bandini, S ;

Sarti, GC .

AICHE JOURNAL, 1999, 45 (07) :1422-1433

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