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Application of Desalination Membranes to Nuclide (Cs, Sr, and Co) Separation
[Image: see text] Desalination and nuclide separation, with cesium (Cs), strontium (Sr), and cobalt (Co), using commercial polymeric membranes are investigated under room temperature (298 K) to elucidate the permeation mechanism and possibility of applying commercial membranes to the separation of r...
Autores principales: | , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American Chemical Society
2020
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Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7439396/ https://www.ncbi.nlm.nih.gov/pubmed/32832779 http://dx.doi.org/10.1021/acsomega.0c02106 |
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author | Kim, Hyung-Ju Kim, Sung-Jun Hyeon, Seungmi Kang, Han Hi Lee, Keun-Young |
author_facet | Kim, Hyung-Ju Kim, Sung-Jun Hyeon, Seungmi Kang, Han Hi Lee, Keun-Young |
author_sort | Kim, Hyung-Ju |
collection | PubMed |
description | [Image: see text] Desalination and nuclide separation, with cesium (Cs), strontium (Sr), and cobalt (Co), using commercial polymeric membranes are investigated under room temperature (298 K) to elucidate the permeation mechanism and possibility of applying commercial membranes to the separation of radioactive nuclides. The physicochemical properties of membranes are characterized by multiple techniques. The thickness of the selective layer and the boundary between the layers of membranes are observed by scanning electron microscopy. The chemical structure of selective and support layers is assessed by direct Fourier transform infrared/attenuated total reflection measurements on membrane samples. Thermogravimetric analysis demonstrates the composition comparison between membranes, which describes the relative amount of selective layers consisting of polyamide. The separation performance of polyamide-based commercial membranes is tested on simulated seawater (35,000 ppm of NaCl) and single- and multi-component aqueous nuclide solutions (10 ppm). Nanofiltration (NF) membranes exhibit a high flux of 160–210 L m(–2) h(–1) with low 31–64% rejection on the permeation of simulated seawater, while reverse osmosis (RO) membranes display a low flux of 13–22 L m(–2) h(–1) with nearly 80% rejection. This reveals RO membranes to be more effective for the rejecting nuclides (Cs, Sr, and Co) in dilute aqueous solutions, and NF membranes have advantage on high throughput. RO membranes reject above 93% for single components and even higher for mixed nuclide separation (>98%), and NF membranes permeate high flux above 230 L m(–2) h(–1). This study indicates that the desalination membranes (NF and RO) can be potential candidates for nuclide separation with combination. |
format | Online Article Text |
id | pubmed-7439396 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2020 |
publisher | American Chemical Society |
record_format | MEDLINE/PubMed |
spelling | pubmed-74393962020-08-21 Application of Desalination Membranes to Nuclide (Cs, Sr, and Co) Separation Kim, Hyung-Ju Kim, Sung-Jun Hyeon, Seungmi Kang, Han Hi Lee, Keun-Young ACS Omega [Image: see text] Desalination and nuclide separation, with cesium (Cs), strontium (Sr), and cobalt (Co), using commercial polymeric membranes are investigated under room temperature (298 K) to elucidate the permeation mechanism and possibility of applying commercial membranes to the separation of radioactive nuclides. The physicochemical properties of membranes are characterized by multiple techniques. The thickness of the selective layer and the boundary between the layers of membranes are observed by scanning electron microscopy. The chemical structure of selective and support layers is assessed by direct Fourier transform infrared/attenuated total reflection measurements on membrane samples. Thermogravimetric analysis demonstrates the composition comparison between membranes, which describes the relative amount of selective layers consisting of polyamide. The separation performance of polyamide-based commercial membranes is tested on simulated seawater (35,000 ppm of NaCl) and single- and multi-component aqueous nuclide solutions (10 ppm). Nanofiltration (NF) membranes exhibit a high flux of 160–210 L m(–2) h(–1) with low 31–64% rejection on the permeation of simulated seawater, while reverse osmosis (RO) membranes display a low flux of 13–22 L m(–2) h(–1) with nearly 80% rejection. This reveals RO membranes to be more effective for the rejecting nuclides (Cs, Sr, and Co) in dilute aqueous solutions, and NF membranes have advantage on high throughput. RO membranes reject above 93% for single components and even higher for mixed nuclide separation (>98%), and NF membranes permeate high flux above 230 L m(–2) h(–1). This study indicates that the desalination membranes (NF and RO) can be potential candidates for nuclide separation with combination. American Chemical Society 2020-08-04 /pmc/articles/PMC7439396/ /pubmed/32832779 http://dx.doi.org/10.1021/acsomega.0c02106 Text en Copyright © 2020 American Chemical Society This is an open access article published under an ACS AuthorChoice License (http://pubs.acs.org/page/policy/authorchoice_termsofuse.html) , which permits copying and redistribution of the article or any adaptations for non-commercial purposes. |
spellingShingle | Kim, Hyung-Ju Kim, Sung-Jun Hyeon, Seungmi Kang, Han Hi Lee, Keun-Young Application of Desalination Membranes to Nuclide (Cs, Sr, and Co) Separation |
title | Application of Desalination Membranes to Nuclide (Cs,
Sr, and Co) Separation |
title_full | Application of Desalination Membranes to Nuclide (Cs,
Sr, and Co) Separation |
title_fullStr | Application of Desalination Membranes to Nuclide (Cs,
Sr, and Co) Separation |
title_full_unstemmed | Application of Desalination Membranes to Nuclide (Cs,
Sr, and Co) Separation |
title_short | Application of Desalination Membranes to Nuclide (Cs,
Sr, and Co) Separation |
title_sort | application of desalination membranes to nuclide (cs,
sr, and co) separation |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7439396/ https://www.ncbi.nlm.nih.gov/pubmed/32832779 http://dx.doi.org/10.1021/acsomega.0c02106 |
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