Developments and future prospects of reverse electrodialysis for salinity gradient power generation: Influence of ion exchange membranes and electrodes

Desalination ◽  
2020 ◽  
Vol 491 ◽  
pp. 114540 ◽  
Author(s):  
Jaewon Jang ◽  
Yesol Kang ◽  
Ji-Hyung Han ◽  
Kyunghoon Jang ◽  
Chang-Min Kim ◽  
...  
Membranes ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 27
Author(s):  
Soroush Mehdizadeh ◽  
Yuriko Kakihana ◽  
Takakazu Abo ◽  
Qingchun Yuan ◽  
Mitsuru Higa

Reverse electrodialysis (RED) is a promising process for harvesting energy from the salinity gradient between two solutions without environmental impacts. Seawater (SW) and river water (RW) are considered the main RED feed solutions because of their good availability. In Okinawa Island (Japan), SW desalination via the reverse osmosis (RO) can be integrated with the RED process due to the production of a large amount of RO brine (concentrated SW, containing ~1 mol/dm3 of NaCl), which is usually discharged directly into the sea. In this study, a pilot-scale RED stack, with 299 cell pairs and 179.4 m2 of effective membrane area, was installed in the SW desalination plant. For the first time, asymmetric monovalent selective membranes with monovalent selective layer just at the side of the membranes were used as the ion exchange membranes (IEMs) inside the RED stack. Natural and model RO brines, as well as SW, were used as the high-concentrate feed solutions. RW, which was in fact surface water in this study and close to the desalination plant, was utilized as the low-concentrate feed solution. The power generation performance investigated by the current-voltage (I–V) test showed the maximum gross power density of 0.96 and 1.46 W/m2 respectively, when the natural and model RO brine/RW were used. These are a 50–60% improvement of the maximum gross power of 0.62 and 0.97 W/m2 generated from the natural and model SW, respectively. The approximate 50% more power generated from the model feed solutions can be assigned to the suppression of concentration polarization of the RED stack due to the absence of multivalent ions.


2021 ◽  
pp. 117255
Author(s):  
Joo-Youn Nam ◽  
Eunjin Jwa ◽  
Hyunji Eom ◽  
Hanki Kim ◽  
Kyosik Hwang ◽  
...  

2015 ◽  
Vol 486 ◽  
pp. 71-88 ◽  
Author(s):  
Jin Gi Hong ◽  
Bopeng Zhang ◽  
Shira Glabman ◽  
Nigmet Uzal ◽  
Xiaomin Dou ◽  
...  

2020 ◽  
Vol MA2020-02 (19) ◽  
pp. 1547-1547
Author(s):  
Lucia Gomez-Coma ◽  
Victor M. Ortiz-Martinez ◽  
Marcos Fallanza ◽  
Alfredo Ortiz Sainz De Aja ◽  
Raquel Ibañez ◽  
...  

Membranes ◽  
2021 ◽  
Vol 11 (8) ◽  
pp. 609
Author(s):  
Hanki Kim ◽  
Jiyeon Choi ◽  
Namjo Jeong ◽  
Yeon-Gil Jung ◽  
Haeun Kim ◽  
...  

The reverse electrodialysis (RED) stack-harnessing salinity gradient power mainly consists of ion exchange membranes (IEMs). Among the various types of IEMs used in RED stacks, pore-filling ion exchange membranes (PIEMs) have been considered promising IEMs to improve the power density of RED stacks. The compositions of PIEMs affect the electrical resistance and permselectivity of PIEMs; however, their effect on the performance of large RED stacks have not yet been considered. In this study, PIEMs of various compositions with respect to the RED stack were adopted to evaluate the performance of the RED stack according to stack size (electrode area: 5 × 5 cm2 vs. 15 × 15 cm2). By increasing the stack size, the gross power per membrane area decreased despite the increase in gross power on a single RED stack. The electrical resistance of the PIEMs was the most important factor for enhancing the power production of the RED stack. Moreover, power production was less sensitive to permselectivities over 90%. By increasing the RED stack size, the contributions of non-ohmic resistances were significantly increased. Thus, we determined that reducing the salinity gradients across PIEMs by ion transport increased the non-ohmic resistance of large RED stacks. These results will aid in designing pilot-scale RED stacks.


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