Nanocomposite and nanostructured ion-exchange membrane in salinity gradient power generation using reverse electrodialysis

Author(s):  
Jin Gi Hong ◽  
Haiping Gao ◽  
Lan Gan ◽  
Xin Tong ◽  
Chengchao Xiao ◽  
...  
2021 ◽  
pp. 117255
Author(s):  
Joo-Youn Nam ◽  
Eunjin Jwa ◽  
Hyunji Eom ◽  
Hanki Kim ◽  
Kyosik Hwang ◽  
...  

Water ◽  
2021 ◽  
Vol 13 (6) ◽  
pp. 814
Author(s):  
Esra Altıok ◽  
Tuğçe Zeynep Kaya ◽  
Enver Güler ◽  
Nalan Kabay ◽  
Marek Bryjak

Salinity gradient energy is a prominent alternative and maintainable energy source, which has considerable potential. Reverse electrodialysis (RED) is one of the most widely studied methods to extract this energy. Despite the considerable progress in research, optimization of RED process is still ongoing. In this study, effects of the number of membrane pairs, ratio of salinity gradient and feed velocity on power generation via the reverse electrodialysis (RED) system were investigated by using Fujifilm cation exchange membrane (CEM Type 2) and FujiFilm anion exchange membrane (AEM Type 2) ion exchange membranes. In the literature, there is no previous study based on a RED system equipped with Fujifilm AEM Type II and CEM Type II membranes that have homogeneous bulk structure. Using 400 µm of intermembrane distance, maximum obtainable power density by 5 pairs of Fujifilm membranes at 1:45 salinity ratio and with a linear flow rate of 0.833 cm/s was 0.426 W/m2.


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.


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