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A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production

Membrane-less electrolyzers utilize fluidic forces instead of solid barriers for the separation of electrolysis gas products. These electrolyzers have low ionic resistance, a simple design, and the ability to work with electrolytes at different pH values. However, the interelectrode distance and the...

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Autores principales: Hadikhani, Pooria, Hashemi, S. Mohammad H., Schenk, Steven A., Psaltis, Demetri
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2021
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8095110/
https://www.ncbi.nlm.nih.gov/pubmed/33997295
http://dx.doi.org/10.1039/d1se00255d
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author Hadikhani, Pooria
Hashemi, S. Mohammad H.
Schenk, Steven A.
Psaltis, Demetri
author_facet Hadikhani, Pooria
Hashemi, S. Mohammad H.
Schenk, Steven A.
Psaltis, Demetri
author_sort Hadikhani, Pooria
collection PubMed
description Membrane-less electrolyzers utilize fluidic forces instead of solid barriers for the separation of electrolysis gas products. These electrolyzers have low ionic resistance, a simple design, and the ability to work with electrolytes at different pH values. However, the interelectrode distance and the flow velocity should be large at high production rates to prevent gas cross over. This is not energetically favorable as the ionic resistance is higher at larger interelectrode distances and the required pumping power increases with the flow velocity. In this work, a new solution is introduced to increase the throughput of electrolyzers without the need for increasing these two parameters. The new microfluidic reactor has three channels separated by porous walls. The electrolyte enters the middle channel and flows into the outer channels through the wall pores. Gas products are being produced in the outer channels. Hydrogen cross over is 0.14% in this electrolyzer at flow rate = 80 mL h(−1) and current density (j) = 300 mA cm(−2). This cross over is 58 times lower than hydrogen cross over in an equivalent membrane-less electrolyzer with parallel electrodes under the same working conditions. Moreover, the addition of a surfactant to the electrolyte further reduces the hydrogen cross over by 21% and the overpotential by 1.9%. This is due to the positive effects of surfactants on the detachment and coalescence dynamics of bubbles. The addition of the passive additive and implementation of the porous walls result in twice the hydrogen production rate in the new reactor compared to parallel electrode electrolyzers with similar hydrogen cross over.
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spelling pubmed-80951102021-05-13 A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production Hadikhani, Pooria Hashemi, S. Mohammad H. Schenk, Steven A. Psaltis, Demetri Sustain Energy Fuels Chemistry Membrane-less electrolyzers utilize fluidic forces instead of solid barriers for the separation of electrolysis gas products. These electrolyzers have low ionic resistance, a simple design, and the ability to work with electrolytes at different pH values. However, the interelectrode distance and the flow velocity should be large at high production rates to prevent gas cross over. This is not energetically favorable as the ionic resistance is higher at larger interelectrode distances and the required pumping power increases with the flow velocity. In this work, a new solution is introduced to increase the throughput of electrolyzers without the need for increasing these two parameters. The new microfluidic reactor has three channels separated by porous walls. The electrolyte enters the middle channel and flows into the outer channels through the wall pores. Gas products are being produced in the outer channels. Hydrogen cross over is 0.14% in this electrolyzer at flow rate = 80 mL h(−1) and current density (j) = 300 mA cm(−2). This cross over is 58 times lower than hydrogen cross over in an equivalent membrane-less electrolyzer with parallel electrodes under the same working conditions. Moreover, the addition of a surfactant to the electrolyte further reduces the hydrogen cross over by 21% and the overpotential by 1.9%. This is due to the positive effects of surfactants on the detachment and coalescence dynamics of bubbles. The addition of the passive additive and implementation of the porous walls result in twice the hydrogen production rate in the new reactor compared to parallel electrode electrolyzers with similar hydrogen cross over. The Royal Society of Chemistry 2021-03-15 /pmc/articles/PMC8095110/ /pubmed/33997295 http://dx.doi.org/10.1039/d1se00255d Text en This journal is © The Royal Society of Chemistry https://creativecommons.org/licenses/by-nc/3.0/
spellingShingle Chemistry
Hadikhani, Pooria
Hashemi, S. Mohammad H.
Schenk, Steven A.
Psaltis, Demetri
A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
title A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
title_full A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
title_fullStr A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
title_full_unstemmed A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
title_short A membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
title_sort membrane-less electrolyzer with porous walls for high throughput and pure hydrogen production
topic Chemistry
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8095110/
https://www.ncbi.nlm.nih.gov/pubmed/33997295
http://dx.doi.org/10.1039/d1se00255d
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