Techno-economic comparison of membrane distillation and MVC in a zero liquid discharge application

被引:130
作者
Schwantes, R. [1 ,2 ,3 ]
Chavan, K. [1 ]
Winter, D. [4 ]
Felsmann, C. [2 ]
Pfafferott, J. [3 ]
机构
[1] SolarSpring GmbH, Christaweg 40, D-79114 Freiburg, Germany
[2] Tech Univ Dresden, Dresden, Germany
[3] Offenburg Univ Appl Sci, Offenburg, Germany
[4] Fraunhofer Inst Solar Energy Syst, Freiberg, Germany
关键词
Membrane distillation; Zero liquid discharge; System design; Techno-economic analysis; HIGH SALINITY; DESIGN; DRIVEN; WATER; MD;
D O I
10.1016/j.desal.2017.11.026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Membrane distillation (MD) is a thermally driven membrane process for the separation of vapour from a liquid stream through a hydrophobic, microporous membrane. However, a commercial breakthrough on a large scale has not been achieved so far. Specific developments on MD technology are required to adapt the technology for applications in which its properties can potentially outshine state of the art technologies such as standard evaporation. In order to drive these developments in a focused manner, firstly it must be shown that MD can be economically attractive in comparison to state of the art systems. Thus, this work presents a technological design and economic analysis for AGMD and v-AGMD for application in a zero liquid discharge (ZLD) process chain and compares it to the costs of mechanical vapour compression (MVC) for the same application. The results show that MD can potentially be similar to 40% more cost effective than MVC for a system capacity of 100 m(3)/day feed water, and up to similar to 75% more cost effective if the MD is driven with free waste heat.
引用
收藏
页码:50 / 68
页数:19
相关论文
共 60 条
[1]   Improving the performance of the air gap membrane distillation process by using a supplementary vacuum pump [J].
Abu-Zeid, Mostafa Abd El-Rady ;
Zhang, Lin ;
Jin, Wang-Yong ;
Feng, Tao ;
Wu, Yier ;
Chen, Huan-Lin ;
Hou, Li'an .
DESALINATION, 2016, 384 :31-42
[2]   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
[3]   Transport analysis of air-gap membrane distillation [J].
Alklaibi, AM ;
Lior, N .
JOURNAL OF MEMBRANE SCIENCE, 2005, 255 (1-2) :239-253
[4]  
Allchudhiri A., 2012, DESALINATION, V287
[5]   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
[6]  
[Anonymous], 2015, THESIS
[7]  
[Anonymous], 2009, RECLAMATION MANAGING
[8]   Concentration of must through vacuum membrane distillation [J].
Bandini, S ;
Sarti, GC .
DESALINATION, 2002, 149 (1-3) :253-259
[9]  
Bodell B.R., 1963, US Patent Application, Patent No. [285,032, 285032]
[10]   Direct contact membrane distillation: Capability to treat hyper-saline solution [J].
Bouchrit, Raja ;
Boubakri, Ali ;
Hafiane, Amor ;
Bouguecha, Salah Al-Tahar .
DESALINATION, 2015, 376 :117-129