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Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation

Oil and gas industries produce a huge amount of wastewater known as produced water which contains diverse contaminants including salts, dissolved organics, dispersed oils, and solids making separation and purification challenging. The chemical and thermal stability of graphene oxide (GO) membranes m...

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Autores principales: Almarzooqi, Khalfan, Ashrafi, Mursal, Kanthan, Theeran, Elkamel, Ali, Pope, Michael A.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2021
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8305078/
https://www.ncbi.nlm.nih.gov/pubmed/34206908
http://dx.doi.org/10.3390/membranes11070475
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author Almarzooqi, Khalfan
Ashrafi, Mursal
Kanthan, Theeran
Elkamel, Ali
Pope, Michael A.
author_facet Almarzooqi, Khalfan
Ashrafi, Mursal
Kanthan, Theeran
Elkamel, Ali
Pope, Michael A.
author_sort Almarzooqi, Khalfan
collection PubMed
description Oil and gas industries produce a huge amount of wastewater known as produced water which contains diverse contaminants including salts, dissolved organics, dispersed oils, and solids making separation and purification challenging. The chemical and thermal stability of graphene oxide (GO) membranes make them promising for use in membrane pervaporation, which may provide a more economical route to purifying this water for disposal or re-use compared to other membrane-based separation techniques. In this study, we investigate the performance and stability of GO membranes cast onto polyethersulfone (PES) supports in the separation of simulated produced water containing high salinity brackish water (30 g/L NaCl) contaminated with phenol, cresol, naphthenic acid, and an oil-in-water emulsion. The GO/PES membranes achieve water flux as high as 47.8 L m(−2) h(−1) for NaCl solutions for membranes operated at 60 °C, while being able to reject 99.9% of the salt and upwards of 56% of the soluble organic components. The flux for membranes tested in pure water, salt, and simulated produced water was found to decrease over 72 h of testing but only to 50–60% of the initial flux in the worst-case scenario. This drop was concurrent with an increase in contact angle and C/O ratio indicating that the GO may become partially reduced during the separation process. Additionally, a closer look at the membrane crosslinker (Zn(2+)) was investigated and found to hydrolyze over time to Zn(OH)(2) with much of it being washed away during the long-term pervaporation.
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spelling pubmed-83050782021-07-25 Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation Almarzooqi, Khalfan Ashrafi, Mursal Kanthan, Theeran Elkamel, Ali Pope, Michael A. Membranes (Basel) Article Oil and gas industries produce a huge amount of wastewater known as produced water which contains diverse contaminants including salts, dissolved organics, dispersed oils, and solids making separation and purification challenging. The chemical and thermal stability of graphene oxide (GO) membranes make them promising for use in membrane pervaporation, which may provide a more economical route to purifying this water for disposal or re-use compared to other membrane-based separation techniques. In this study, we investigate the performance and stability of GO membranes cast onto polyethersulfone (PES) supports in the separation of simulated produced water containing high salinity brackish water (30 g/L NaCl) contaminated with phenol, cresol, naphthenic acid, and an oil-in-water emulsion. The GO/PES membranes achieve water flux as high as 47.8 L m(−2) h(−1) for NaCl solutions for membranes operated at 60 °C, while being able to reject 99.9% of the salt and upwards of 56% of the soluble organic components. The flux for membranes tested in pure water, salt, and simulated produced water was found to decrease over 72 h of testing but only to 50–60% of the initial flux in the worst-case scenario. This drop was concurrent with an increase in contact angle and C/O ratio indicating that the GO may become partially reduced during the separation process. Additionally, a closer look at the membrane crosslinker (Zn(2+)) was investigated and found to hydrolyze over time to Zn(OH)(2) with much of it being washed away during the long-term pervaporation. MDPI 2021-06-26 /pmc/articles/PMC8305078/ /pubmed/34206908 http://dx.doi.org/10.3390/membranes11070475 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
Almarzooqi, Khalfan
Ashrafi, Mursal
Kanthan, Theeran
Elkamel, Ali
Pope, Michael A.
Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation
title Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation
title_full Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation
title_fullStr Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation
title_full_unstemmed Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation
title_short Graphene Oxide Membranes for High Salinity, Produced Water Separation by Pervaporation
title_sort graphene oxide membranes for high salinity, produced water separation by pervaporation
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC8305078/
https://www.ncbi.nlm.nih.gov/pubmed/34206908
http://dx.doi.org/10.3390/membranes11070475
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