An internal-integrated RED/ED system for energy-saving seawater desalination: A model study

被引:17
作者
Chen, Man [1 ]
Mei, Ying [2 ]
Yu, Yuqing [1 ]
Zeng, Raymond Jianxiong [1 ]
Zhang, Fang [1 ]
Zhou, Shungui [1 ]
Tang, Chuyang Y. [2 ]
机构
[1] Fujian Agr & Forestry Univ, Fujian Prov Key Lab Soil Environm Hlth & Regulat, Coll Resources & Environm, Fuzhou 350002, Fujian, Peoples R China
[2] Univ Hong Kong, Dept Civil Engn, Pokfulam, Hong Kong 999077, Peoples R China
基金
中国国家自然科学基金;
关键词
Desalination; Electrodialysis; Reverse electrodialysis; Hybrid system; Modeling; ELECTRODIALYSIS PILOT-PLANT; REVERSE ELECTRODIALYSIS; SALINE WATERS; POWER PRODUCTION; RIVER WATER; PERFORMANCE; TECHNOLOGY; RECOVERY; OSMOSIS; DESIGN;
D O I
10.1016/j.energy.2018.12.111
中图分类号
O414.1 [热力学];
学科分类号
摘要
Salinity gradient energy extracting by a reverse electrodialysis (RED) unit using for electrodialysis (ED) desalination process is a potential way to achieve energy-economic and sustainable production of freshwater. However, the parameters in RED and ED unit synergistically influence the desalination process, resulting to the hybrid process controlled by multi-parameters. Modeling of an RED/ED is a simple way to describe the desalination process and reveal the effects of these parameters on the performance of system and then to find the better adaption of RED/ED. In this study, a model of an internal integrated RED/ED hybrid system is first established. It found that the ratio of desalination in RED/ED is higher than 90%. The brine/river is the alternative combination to realize seawater desalination with a desalination rate of 0.38 h m(2)/mol. The desalination capacity of RED/ED (0.43-2.6 mol/h-m(2)) is much higher than that of the external-integrated RED + ED system (0.10-0.15 mol/h.m(2)), but it is of simpler configuration and has a lower energy requirement. Moreover, the RED/ED system is preferred for using in the pre-desalination process. The outcome of this model is helpful in the design of practical RED/ED systems, and points out the development potential of RED/ED in practical applications. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:139 / 148
页数:10
相关论文
共 36 条
[1]   Energy consumption and water production cost of conventional and renewable-energy-powered desalination processes [J].
Al-Karaghouli, Ali ;
Kazmerski, Lawrence L. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2013, 24 :343-356
[2]   Membrane technology in renewable-energy-driven desalination [J].
Ali, Aamer ;
Tufa, Ramato Ashu ;
Macedonio, Francesca ;
Curcio, Efrem ;
Drioli, Enrico .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 81 :1-21
[3]   Reverse Electrodialysis for energy production from natural river water and seawater [J].
Avci, Ahmet H. ;
Tufa, Ramato A. ;
Fontananova, Enrica ;
Di Profio, Gianluca ;
Curcio, Efrem .
ENERGY, 2018, 165 :512-521
[4]   Reverse electrodialysis with NH4HCO3-water systems for heat-to-power conversion [J].
Bevacqua, M. ;
Tamburini, A. ;
Papapetrou, M. ;
Cipollina, A. ;
Micale, G. ;
Piacentino, A. .
ENERGY, 2017, 137 :1293-1307
[5]   Entropy generation analysis of electrodialysis [J].
Chehayeb, Karim M. ;
Lienhard, John H. .
DESALINATION, 2017, 413 :184-198
[6]   Energy self-sufficient desalination stack as a potential fresh water supply on small islands [J].
Chen, Qing ;
Liu, Yuan-Yuan ;
Xue, Chang ;
Yang, Yu-Ling ;
Zhang, Wei-Ming .
DESALINATION, 2015, 359 :52-58
[7]   An electrodialysis model for determination of the optimal current density [J].
Choi, EY ;
Choi, JH ;
Moon, SH .
DESALINATION, 2003, 153 (1-3) :399-404
[8]   Batch ED fed by a PV unit: a reliable, flexible, and sustainable integration [J].
Cirez, F. ;
Uche, J. ;
Bayod, A. A. ;
Martinez, A. .
DESALINATION AND WATER TREATMENT, 2013, 51 (4-6) :673-685
[9]   Experimentally obtainable energy from mixing river water, seawater or brines with reverse electrodialysis [J].
Daniilidis, Alexandros ;
Vermaas, David A. ;
Herber, Rien ;
Nijmeijer, Kitty .
RENEWABLE ENERGY, 2014, 64 :123-131
[10]   Optimal design of experiments for parameter identification in electrodialysis models [J].
Galvanin, Federico ;
Marchesini, Raffaele ;
Barolo, Massimiliano ;
Bezzo, Fabrizio ;
Fidaleo, Marcello .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2016, 105 :107-119