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Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries

Demand for nickel and cobalt sulfate is expected to increase due to the rapidly growing Li-battery industry needed for the electrification of automobiles. This has led to an increase in the production of sodium sulfate as a waste effluent that needs to be processed to meet discharge guidelines. Usin...

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Autores principales: Kuldeep, Badenhorst, Wouter Dirk, Kauranen, Pertti, Pajari, Heikki, Ruismäki, Ronja, Mannela, Petri, Murtomäki, Lasse
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2021
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8468557/
https://www.ncbi.nlm.nih.gov/pubmed/34564535
http://dx.doi.org/10.3390/membranes11090718
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author Kuldeep,
Badenhorst, Wouter Dirk
Kauranen, Pertti
Pajari, Heikki
Ruismäki, Ronja
Mannela, Petri
Murtomäki, Lasse
author_facet Kuldeep,
Badenhorst, Wouter Dirk
Kauranen, Pertti
Pajari, Heikki
Ruismäki, Ronja
Mannela, Petri
Murtomäki, Lasse
author_sort Kuldeep,
collection PubMed
description Demand for nickel and cobalt sulfate is expected to increase due to the rapidly growing Li-battery industry needed for the electrification of automobiles. This has led to an increase in the production of sodium sulfate as a waste effluent that needs to be processed to meet discharge guidelines. Using bipolar membrane electrodialysis (BPED), acids and bases can be effectively produced from corresponding salts found in these waste effluents. However, the efficiency and environmental sustainability of the overall BPED process depends upon several factors, including the properties of the ion exchange membranes employed, effluent type, and temperature which affects the viscosity and conductivity of feed effluent, and the overpotentials. This work focuses on the recycling of Na(2)SO(4) rich waste effluent, through a feed and bleed BPED process. A high ion-exchange capacity and ionic conductivity with excellent stability up to 41 °C is observed during the proposed BPED process, with this temperature increase also leading to improved current efficiency. Five and ten repeating units were tested to determine the effect on BPED stack performance, as well as the effect of temperature and current density on the stack voltage and current efficiency. Furthermore, the concentration and maximum purity (>96.5%) of the products were determined. Using the experimental data, both the capital expense (CAPEX) and operating expense (OPEX) for a theoretical plant capacity of 100 m(3) h(−1) of Na(2)SO(4) at 110 g L(−1) was calculated, yielding CAPEX values of 20 M EUR, and OPEX at 14.2 M EUR/year with a payback time of 11 years, however, the payback time is sensitive to chemical and electricity prices.
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spelling pubmed-84685572021-09-27 Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries Kuldeep, Badenhorst, Wouter Dirk Kauranen, Pertti Pajari, Heikki Ruismäki, Ronja Mannela, Petri Murtomäki, Lasse Membranes (Basel) Article Demand for nickel and cobalt sulfate is expected to increase due to the rapidly growing Li-battery industry needed for the electrification of automobiles. This has led to an increase in the production of sodium sulfate as a waste effluent that needs to be processed to meet discharge guidelines. Using bipolar membrane electrodialysis (BPED), acids and bases can be effectively produced from corresponding salts found in these waste effluents. However, the efficiency and environmental sustainability of the overall BPED process depends upon several factors, including the properties of the ion exchange membranes employed, effluent type, and temperature which affects the viscosity and conductivity of feed effluent, and the overpotentials. This work focuses on the recycling of Na(2)SO(4) rich waste effluent, through a feed and bleed BPED process. A high ion-exchange capacity and ionic conductivity with excellent stability up to 41 °C is observed during the proposed BPED process, with this temperature increase also leading to improved current efficiency. Five and ten repeating units were tested to determine the effect on BPED stack performance, as well as the effect of temperature and current density on the stack voltage and current efficiency. Furthermore, the concentration and maximum purity (>96.5%) of the products were determined. Using the experimental data, both the capital expense (CAPEX) and operating expense (OPEX) for a theoretical plant capacity of 100 m(3) h(−1) of Na(2)SO(4) at 110 g L(−1) was calculated, yielding CAPEX values of 20 M EUR, and OPEX at 14.2 M EUR/year with a payback time of 11 years, however, the payback time is sensitive to chemical and electricity prices. MDPI 2021-09-18 /pmc/articles/PMC8468557/ /pubmed/34564535 http://dx.doi.org/10.3390/membranes11090718 Text en © 2021 by the authors. https://creativecommons.org/licenses/by/4.0/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 (https://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Kuldeep,
Badenhorst, Wouter Dirk
Kauranen, Pertti
Pajari, Heikki
Ruismäki, Ronja
Mannela, Petri
Murtomäki, Lasse
Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries
title Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries
title_full Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries
title_fullStr Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries
title_full_unstemmed Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries
title_short Bipolar Membrane Electrodialysis for Sulfate Recycling in the Metallurgical Industries
title_sort bipolar membrane electrodialysis for sulfate recycling in the metallurgical industries
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8468557/
https://www.ncbi.nlm.nih.gov/pubmed/34564535
http://dx.doi.org/10.3390/membranes11090718
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