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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...
Autores principales: | , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2021
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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. |
format | Online Article Text |
id | pubmed-8468557 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2021 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
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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