Simulation of Vacuum Membrane Distillation Process for Desalination with Aspen Plus

被引:11
|
作者
Cao, Wensheng [1 ,2 ,3 ]
Mujtaba, Iqbal M. [4 ]
机构
[1] Jimei Univ, Coll Mech & Energy Engn, Xiamen 361021, Peoples R China
[2] Fujian Prov Key Lab Energy Cleaning Utilizat & De, Xiamen 361021, Peoples R China
[3] Cleaning Combust & Energy Utilizat Res Ctr Fujian, Xiamen 361021, Peoples R China
[4] Univ Bradford, Sch Engn & Informat, Bradford BD7 1DP, W Yorkshire, England
关键词
DIRECT-CONTACT; HEAT-TRANSFER; MASS-TRANSFER; VMD; OPTIMIZATION; MODELS;
D O I
10.1021/ie502874c
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This paper presents a simulation study of vacuum membrane distillation (VMD) for desalination. A simulation model was built on the Aspen Plus platform as a user defined unit operation for the VMD module. A simplified mathematical model was verified, and the analysis of process performance based on simulation was also carried out. Temperature and concentration polarization effects are significant in the conditions of higher feed temperature and/or vacuum pressure. The sign of (P-I,P-f - P-I,P-p), difference of the vapor pressures between the membranes at the interfaces, is an indicator of the vacuum pressure threshold. Increasing the vacuum pressure at lower feed temperature is an effective way to increase the permeate flux and reduce the energy consumption simultaneously.
引用
收藏
页码:672 / 680
页数:9
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