Theoretical modeling of direct contact membrane distillation (DCMD): effects of operation parameters on flux

被引：16

作者：

Kamrani, Parisa Moghaddam ^{[1
]}

Bakhtiari, Omid ^{[2
]}

Kazemi, Pezhman ^{[3
]}

Mohammadi, Toraj ^{[1
]}

机构：

[1] Islamic Azad Univ, Dept Chem Engn, South Tehran Branch, Tehran, Iran

[2] Razi Univ, Dept Chem Engn, Kermanshah 6714967346, Iran

[3] Jagiellonian Univ, Coll Med, Fac Pharm, Dept Pharmaceut Technol & Biopharmaceut, PL-30688 Krakow, Poland

来源：

DESALINATION AND WATER TREATMENT | 2015年 / 56卷 / 08期

关键词：

Direct contact membrane distillation; Mathematical model; Flux prediction; Temperature polarization; MONTE-CARLO-SIMULATION; MASS-TRANSFER; HEAT; DESALINATION; ENHANCEMENT; TRANSPORT; SURFACE; MD;

D O I：

10.1080/19443994.2014.960461

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

In this research, a mathematical model for calculating and predicting flux through direct contact membrane distillation in flat-sheet membrane modules was presented. The membrane properties' and permeate and feed streams' main specifications were considered as model input parameters. The effects of simultaneous heat and mass transfer were investigated. The developed mathematical model was written in Visual Basic language based on heat and mass balances. The influences of process parameters such as temperature, flow rate, feed concentration, and membrane properties (pore size) on flux and temperature polarization coefficient were evaluated by the model. The modeling results were compared with some experimental data and good agreement was observed.

引用

页码：2013 / 2022

页数：10

共 27 条

[1] Membrane distillation: A comprehensive review [J].

Alkhudhiri, Abdullah ;

Darwish, Naif ;

Hilal, Nidal .

DESALINATION, 2012, 287 :2-18

[2] Heat and mass transfer resistance analysis of membrane distillation [J].

Alklaibi, A. M. ;

Lior, Noam .

JOURNAL OF MEMBRANE SCIENCE, 2006, 282 (1-2) :362-369

[3] Membrane-distillation desalination: status and potential [J].

Alklaibi, AM ;

Lior, N .

DESALINATION, 2005, 171 (02) :111-131

[4] An experimentally optimized model for heat and mass transfer in direct contact membrane distillation [J].

Andrjesdottir, Oloef ;

Ong, Chin Lee ;

Nabavi, Majid ;

Paredes, Stephan ;

Khalil, A. S. G. ;

Michel, Bruno ;

Poulikakos, Dimos .

INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2013, 66 :855-867

[5] Modelling the simultaneous heat and mass transfer of direct contact membrane distillation in hollow fibre modules [J].

Bui, V. A. ;

Vu, L. T. T. ;

Nguyen, M. H. .

JOURNAL OF MEMBRANE SCIENCE, 2010, 353 (1-2) :85-93

[6] Experimental study of desalination using direct contact membrane distillation: a new approach to flux enhancement [J].

Cath, TY ;

Adams, VD ;

Childress, AE .

JOURNAL OF MEMBRANE SCIENCE, 2004, 228 (01) :5-16

[7] Membrane distillation and related operations - A review [J].

Curcio, E ;

Drioli, E .

SEPARATION AND PURIFICATION REVIEWS, 2005, 34 (01) :35-86

[8] 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

[9] Theoretical and experimental studies of flux enhancement with roughened surface in direct contact membrane distillation desalination [J].

Ho, Chii-Dong ;

Chang, Hsuan ;

Chang, Cheng-Liang ;

Huang, Cheng-Hao .

JOURNAL OF MEMBRANE SCIENCE, 2013, 433 :160-166

[10] Direct contact membrane distillation (DCMD): Experimental study on the commercial PTFE membrane and modeling [J].

Hwang, Ho Jung ;

He, Ke ;

Gray, Stephen ;

Zhang, Jianhua ;

Moon, Il Shik .

JOURNAL OF MEMBRANE SCIENCE, 2011, 371 (1-2) :90-98

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