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The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate

The ohmic resistances of the anion and cation ion-exchange membranes (IEMs) that constitute a reverse electrodialysis system (RED) are of crucial importance for its performance. In this work, we study the influence of concentration (0.1 M, 0.5 M, 1 M and 2 M) of ammonium bicarbonate solutions on the...

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Autores principales: Raka, Yash Dharmendra, Bock, Robert, Karoliussen, Håvard, Wilhelmsen, Øivind, Stokke Burheim, Odne
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2021
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7919660/
https://www.ncbi.nlm.nih.gov/pubmed/33669178
http://dx.doi.org/10.3390/membranes11020135
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author Raka, Yash Dharmendra
Bock, Robert
Karoliussen, Håvard
Wilhelmsen, Øivind
Stokke Burheim, Odne
author_facet Raka, Yash Dharmendra
Bock, Robert
Karoliussen, Håvard
Wilhelmsen, Øivind
Stokke Burheim, Odne
author_sort Raka, Yash Dharmendra
collection PubMed
description The ohmic resistances of the anion and cation ion-exchange membranes (IEMs) that constitute a reverse electrodialysis system (RED) are of crucial importance for its performance. In this work, we study the influence of concentration (0.1 M, 0.5 M, 1 M and 2 M) of ammonium bicarbonate solutions on the ohmic resistances of ten commercial IEMs. We also studied the ohmic resistance at elevated temperature 313 K. Measurements have been performed with a direct two-electrode electrochemical impedance spectroscopy (EIS) method. As the ohmic resistance of the IEMs depends linearly on the membrane thickness, we measured the impedance for three different layered thicknesses, and the results were normalised. To gauge the role of the membrane resistances in the use of RED for production of hydrogen by use of waste heat, we used a thermodynamic and an economic model to study the impact of the ohmic resistance of the IEMs on hydrogen production rate, waste heat required, thermochemical conversion efficiency and the levelised cost of hydrogen. The highest performance was achieved with a stack made of FAS30 and CSO Type IEMs, producing hydrogen at 8.48× 10 [Formula: see text] kg m [Formula: see text] s [Formula: see text] with a waste heat requirement of 344 kWh kg [Formula: see text] hydrogen. This yielded an operating efficiency of 9.7% and a levelised cost of 7.80 € kg [Formula: see text].
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spelling pubmed-79196602021-03-02 The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate Raka, Yash Dharmendra Bock, Robert Karoliussen, Håvard Wilhelmsen, Øivind Stokke Burheim, Odne Membranes (Basel) Article The ohmic resistances of the anion and cation ion-exchange membranes (IEMs) that constitute a reverse electrodialysis system (RED) are of crucial importance for its performance. In this work, we study the influence of concentration (0.1 M, 0.5 M, 1 M and 2 M) of ammonium bicarbonate solutions on the ohmic resistances of ten commercial IEMs. We also studied the ohmic resistance at elevated temperature 313 K. Measurements have been performed with a direct two-electrode electrochemical impedance spectroscopy (EIS) method. As the ohmic resistance of the IEMs depends linearly on the membrane thickness, we measured the impedance for three different layered thicknesses, and the results were normalised. To gauge the role of the membrane resistances in the use of RED for production of hydrogen by use of waste heat, we used a thermodynamic and an economic model to study the impact of the ohmic resistance of the IEMs on hydrogen production rate, waste heat required, thermochemical conversion efficiency and the levelised cost of hydrogen. The highest performance was achieved with a stack made of FAS30 and CSO Type IEMs, producing hydrogen at 8.48× 10 [Formula: see text] kg m [Formula: see text] s [Formula: see text] with a waste heat requirement of 344 kWh kg [Formula: see text] hydrogen. This yielded an operating efficiency of 9.7% and a levelised cost of 7.80 € kg [Formula: see text]. MDPI 2021-02-16 /pmc/articles/PMC7919660/ /pubmed/33669178 http://dx.doi.org/10.3390/membranes11020135 Text en © 2021 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Raka, Yash Dharmendra
Bock, Robert
Karoliussen, Håvard
Wilhelmsen, Øivind
Stokke Burheim, Odne
The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate
title The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate
title_full The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate
title_fullStr The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate
title_full_unstemmed The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate
title_short The Influence of Concentration and Temperature on the Membrane Resistance of Ion Exchange Membranes and the Levelised Cost of Hydrogen from Reverse Electrodialysis with Ammonium Bicarbonate
title_sort influence of concentration and temperature on the membrane resistance of ion exchange membranes and the levelised cost of hydrogen from reverse electrodialysis with ammonium bicarbonate
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7919660/
https://www.ncbi.nlm.nih.gov/pubmed/33669178
http://dx.doi.org/10.3390/membranes11020135
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