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Upscaling Reverse Electrodialysis

[Image: see text] Salinity gradient energy is a sustainable, renewable, and clean energy source. When waters with different salinities are mixed, the change in Gibbs free energy can be harvested as energy and only brackish water remains. Reverse electrodialysis is one of the technologies that can ha...

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Autores principales: Moreno, Jordi, Grasman, Simon, van Engelen, Ronny, Nijmeijer, Kitty
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2018
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6146319/
https://www.ncbi.nlm.nih.gov/pubmed/30102521
http://dx.doi.org/10.1021/acs.est.8b01886
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author Moreno, Jordi
Grasman, Simon
van Engelen, Ronny
Nijmeijer, Kitty
author_facet Moreno, Jordi
Grasman, Simon
van Engelen, Ronny
Nijmeijer, Kitty
author_sort Moreno, Jordi
collection PubMed
description [Image: see text] Salinity gradient energy is a sustainable, renewable, and clean energy source. When waters with different salinities are mixed, the change in Gibbs free energy can be harvested as energy and only brackish water remains. Reverse electrodialysis is one of the technologies that can harvest this sustainable energy source. High power densities have been obtained in small lab scale systems, but translation to large industrial scale stacks is essential for commercialization of the technology. Moreover, power density is an important parameter, and efficiency, i.e., the amount of energy harvested compared to the amount of energy available in the feed waters, is critical for commercial processes. In this work, we systematically investigate the influence of stack size and membrane type on power density, thermodynamic efficiency, and energy efficiency. Results show that the residence time is an excellent parameter for comparing differently sized stacks and translating lab scale experimental results to larger pilot stacks. Also, the influence of undesired water permeability and co-ion diffusion (as reflected in permselectivity) is clearly visible when measuring the thermodynamic efficiency. An averaged thermodynamic efficiency of 44.9% is measured using Fujifilm Type 10 anion exchange and cation exchange membranes that have low water permeability and high permselectivity. This value comes close to the thermodynamic maximum of 50%.
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spelling pubmed-61463192018-09-21 Upscaling Reverse Electrodialysis Moreno, Jordi Grasman, Simon van Engelen, Ronny Nijmeijer, Kitty Environ Sci Technol [Image: see text] Salinity gradient energy is a sustainable, renewable, and clean energy source. When waters with different salinities are mixed, the change in Gibbs free energy can be harvested as energy and only brackish water remains. Reverse electrodialysis is one of the technologies that can harvest this sustainable energy source. High power densities have been obtained in small lab scale systems, but translation to large industrial scale stacks is essential for commercialization of the technology. Moreover, power density is an important parameter, and efficiency, i.e., the amount of energy harvested compared to the amount of energy available in the feed waters, is critical for commercial processes. In this work, we systematically investigate the influence of stack size and membrane type on power density, thermodynamic efficiency, and energy efficiency. Results show that the residence time is an excellent parameter for comparing differently sized stacks and translating lab scale experimental results to larger pilot stacks. Also, the influence of undesired water permeability and co-ion diffusion (as reflected in permselectivity) is clearly visible when measuring the thermodynamic efficiency. An averaged thermodynamic efficiency of 44.9% is measured using Fujifilm Type 10 anion exchange and cation exchange membranes that have low water permeability and high permselectivity. This value comes close to the thermodynamic maximum of 50%. American Chemical Society 2018-08-13 2018-09-18 /pmc/articles/PMC6146319/ /pubmed/30102521 http://dx.doi.org/10.1021/acs.est.8b01886 Text en Copyright © 2018 American Chemical Society This is an open access article published under a Creative Commons Non-Commercial No Derivative Works (CC-BY-NC-ND) Attribution License (http://pubs.acs.org/page/policy/authorchoice_ccbyncnd_termsofuse.html) , which permits copying and redistribution of the article, and creation of adaptations, all for non-commercial purposes.
spellingShingle Moreno, Jordi
Grasman, Simon
van Engelen, Ronny
Nijmeijer, Kitty
Upscaling Reverse Electrodialysis
title Upscaling Reverse Electrodialysis
title_full Upscaling Reverse Electrodialysis
title_fullStr Upscaling Reverse Electrodialysis
title_full_unstemmed Upscaling Reverse Electrodialysis
title_short Upscaling Reverse Electrodialysis
title_sort upscaling reverse electrodialysis
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC6146319/
https://www.ncbi.nlm.nih.gov/pubmed/30102521
http://dx.doi.org/10.1021/acs.est.8b01886
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