Electro dialysis reversal (EDR) performance for reject brine treatment of reverse osmosis desalination system
In this study, the performance of bench-scale EDR was evaluated using the samples taken from the 1st and the 2nd stage RO from the Brackish Water Reverse Osmosis (BWRO) plant in Eshtehard, Iran. The measurements indicated that original TDS of the aquifer brackish water was equal to 3,229–3,664 mg/L,...
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| creator | Ataei Far, Hossein Hassani, Amir Hessam Taghavi, Lobat Fazeli, Mojtaba Rashidi Mehrabadi, Abdollah |
| description | In this study, the performance of bench-scale EDR was evaluated using the samples taken from the 1st and the 2nd stage RO from the Brackish Water Reverse Osmosis (BWRO) plant in Eshtehard, Iran. The measurements indicated that original TDS of the aquifer brackish water was equal to 3,229–3,664 mg/L, whereas TDS of the 1
st
stage RO brine was between 5,500 and 7,700 mg/L, that TDS of the 2
nd
stage RO brine was in the range of 9,500–10,600 mg/L. A batch bench-scale EDR system of 12 l/h was used with a direct electric current at three different scenarios. In the first, the brine was fed at 20°C (as a reference regulated point). In the second, temperature (14, 20, 26.5°C), and in the third, voltage were changed (6, 12, 18, 24 V) to investigate their influences on performance of the EDR process, while the other operational parameters (feed flow rate, recovery ratio, quality of feed brine)were kept constant. Based on the data analysis using the ANOVA and DUNCAN tests for the second and third scenarios, it was observed that the optimum TDS removal efficiency of the EDR process can be at temperature of 26.5°C and voltage of 18 V. On the other hand, the successful performance of the bench-scale EDR in reducing the 29,000 mg/L TDS and the 45,000 μmhos/cm EC of the 2
nd
stage brine to 1,716 mg/L (TDS) and 2,640 μmhos/cm (EC) (at 26.5°C and 24V) could be considered as the main achievement of this research. Overall, the hybrid process RO-EDR-RO can be considered as the best technical, environmental and economical scenario for the development of Eshtehard Desalination Plant phase 2 at full scale. |
| doi_str_mv | 10.1371/journal.pone.0273240 |
| format | Article |
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st
stage RO brine was between 5,500 and 7,700 mg/L, that TDS of the 2
nd
stage RO brine was in the range of 9,500–10,600 mg/L. A batch bench-scale EDR system of 12 l/h was used with a direct electric current at three different scenarios. In the first, the brine was fed at 20°C (as a reference regulated point). In the second, temperature (14, 20, 26.5°C), and in the third, voltage were changed (6, 12, 18, 24 V) to investigate their influences on performance of the EDR process, while the other operational parameters (feed flow rate, recovery ratio, quality of feed brine)were kept constant. Based on the data analysis using the ANOVA and DUNCAN tests for the second and third scenarios, it was observed that the optimum TDS removal efficiency of the EDR process can be at temperature of 26.5°C and voltage of 18 V. On the other hand, the successful performance of the bench-scale EDR in reducing the 29,000 mg/L TDS and the 45,000 μmhos/cm EC of the 2
nd
stage brine to 1,716 mg/L (TDS) and 2,640 μmhos/cm (EC) (at 26.5°C and 24V) could be considered as the main achievement of this research. Overall, the hybrid process RO-EDR-RO can be considered as the best technical, environmental and economical scenario for the development of Eshtehard Desalination Plant phase 2 at full scale.</description><identifier>ISSN: 1932-6203</identifier><identifier>EISSN: 1932-6203</identifier><identifier>DOI: 10.1371/journal.pone.0273240</identifier><identifier>PMID: 36001606</identifier><language>eng</language><publisher>San Francisco: Public Library of Science</publisher><subject>Aquatic resources ; Aquifers ; Brackish water ; Brines ; Cost recovery ; Data analysis ; Desalination ; Desalination plants ; Dialysis ; Drinking water ; Ecology and Environmental Sciences ; Electric currents ; Electric potential ; Electrodes ; Electrodialysis ; Engineering and Technology ; Evaluation ; Feed quality ; Flow velocity ; Freshwater resources ; Iran ; Management ; Membranes ; Performance evaluation ; Physical Sciences ; Research and Analysis Methods ; Reverse osmosis ; Saline water conversion plants ; Social Sciences ; Variance analysis ; Voltage</subject><ispartof>PloS one, 2022-08, Vol.17 (8), p.e0273240-e0273240</ispartof><rights>COPYRIGHT 2022 Public Library of Science</rights><rights>2022 Ataei Far et al. This is an open access article distributed under the terms of the Creative Commons Attribution License: http://creativecommons.org/licenses/by/4.0/ (the “License”), which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited. Notwithstanding the ProQuest Terms and Conditions, you may use this content in accordance with the terms of the License.</rights><rights>2022 Ataei Far et al 2022 Ataei Far et al</rights><lds50>peer_reviewed</lds50><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c519t-f68ce8770e3542d06b2baef0750ec7f91508866d56e94f8c8e2ce67b7d37312d3</cites><orcidid>0000-0002-4973-318X</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC9401187/pdf/$$EPDF$$P50$$Gpubmedcentral$$Hfree_for_read</linktopdf><linktohtml>$$Uhttps://www.ncbi.nlm.nih.gov/pmc/articles/PMC9401187/$$EHTML$$P50$$Gpubmedcentral$$Hfree_for_read</linktohtml><link.rule.ids>230,314,723,776,780,860,881,2096,2915,23845,27901,27902,53766,53768,79343,79344</link.rule.ids></links><search><creatorcontrib>Ataei Far, Hossein</creatorcontrib><creatorcontrib>Hassani, Amir Hessam</creatorcontrib><creatorcontrib>Taghavi, Lobat</creatorcontrib><creatorcontrib>Fazeli, Mojtaba</creatorcontrib><creatorcontrib>Rashidi Mehrabadi, Abdollah</creatorcontrib><title>Electro dialysis reversal (EDR) performance for reject brine treatment of reverse osmosis desalination system</title><title>PloS one</title><description>In this study, the performance of bench-scale EDR was evaluated using the samples taken from the 1st and the 2nd stage RO from the Brackish Water Reverse Osmosis (BWRO) plant in Eshtehard, Iran. The measurements indicated that original TDS of the aquifer brackish water was equal to 3,229–3,664 mg/L, whereas TDS of the 1
st
stage RO brine was between 5,500 and 7,700 mg/L, that TDS of the 2
nd
stage RO brine was in the range of 9,500–10,600 mg/L. A batch bench-scale EDR system of 12 l/h was used with a direct electric current at three different scenarios. In the first, the brine was fed at 20°C (as a reference regulated point). In the second, temperature (14, 20, 26.5°C), and in the third, voltage were changed (6, 12, 18, 24 V) to investigate their influences on performance of the EDR process, while the other operational parameters (feed flow rate, recovery ratio, quality of feed brine)were kept constant. Based on the data analysis using the ANOVA and DUNCAN tests for the second and third scenarios, it was observed that the optimum TDS removal efficiency of the EDR process can be at temperature of 26.5°C and voltage of 18 V. On the other hand, the successful performance of the bench-scale EDR in reducing the 29,000 mg/L TDS and the 45,000 μmhos/cm EC of the 2
nd
stage brine to 1,716 mg/L (TDS) and 2,640 μmhos/cm (EC) (at 26.5°C and 24V) could be considered as the main achievement of this research. Overall, the hybrid process RO-EDR-RO can be considered as the best technical, environmental and economical scenario for the development of Eshtehard Desalination Plant phase 2 at full scale.</description><subject>Aquatic resources</subject><subject>Aquifers</subject><subject>Brackish water</subject><subject>Brines</subject><subject>Cost recovery</subject><subject>Data analysis</subject><subject>Desalination</subject><subject>Desalination plants</subject><subject>Dialysis</subject><subject>Drinking water</subject><subject>Ecology and Environmental Sciences</subject><subject>Electric currents</subject><subject>Electric potential</subject><subject>Electrodes</subject><subject>Electrodialysis</subject><subject>Engineering and Technology</subject><subject>Evaluation</subject><subject>Feed quality</subject><subject>Flow velocity</subject><subject>Freshwater resources</subject><subject>Iran</subject><subject>Management</subject><subject>Membranes</subject><subject>Performance 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dialysis reversal (EDR) performance for reject brine treatment of reverse osmosis desalination system</title><author>Ataei Far, Hossein ; Hassani, Amir Hessam ; Taghavi, Lobat ; Fazeli, Mojtaba ; Rashidi Mehrabadi, Abdollah</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c519t-f68ce8770e3542d06b2baef0750ec7f91508866d56e94f8c8e2ce67b7d37312d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2022</creationdate><topic>Aquatic resources</topic><topic>Aquifers</topic><topic>Brackish water</topic><topic>Brines</topic><topic>Cost recovery</topic><topic>Data analysis</topic><topic>Desalination</topic><topic>Desalination plants</topic><topic>Dialysis</topic><topic>Drinking water</topic><topic>Ecology and Environmental Sciences</topic><topic>Electric currents</topic><topic>Electric potential</topic><topic>Electrodes</topic><topic>Electrodialysis</topic><topic>Engineering and Technology</topic><topic>Evaluation</topic><topic>Feed quality</topic><topic>Flow velocity</topic><topic>Freshwater resources</topic><topic>Iran</topic><topic>Management</topic><topic>Membranes</topic><topic>Performance evaluation</topic><topic>Physical Sciences</topic><topic>Research and Analysis Methods</topic><topic>Reverse osmosis</topic><topic>Saline water conversion plants</topic><topic>Social Sciences</topic><topic>Variance analysis</topic><topic>Voltage</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ataei Far, Hossein</creatorcontrib><creatorcontrib>Hassani, Amir Hessam</creatorcontrib><creatorcontrib>Taghavi, Lobat</creatorcontrib><creatorcontrib>Fazeli, Mojtaba</creatorcontrib><creatorcontrib>Rashidi Mehrabadi, Abdollah</creatorcontrib><collection>CrossRef</collection><collection>ProQuest Central (Corporate)</collection><collection>Animal Behavior Abstracts</collection><collection>Bacteriology Abstracts (Microbiology 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Academic</collection><collection>PubMed Central (Full Participant titles)</collection><collection>DOAJ Directory of Open Access Journals</collection><jtitle>PloS one</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ataei Far, Hossein</au><au>Hassani, Amir Hessam</au><au>Taghavi, Lobat</au><au>Fazeli, Mojtaba</au><au>Rashidi Mehrabadi, Abdollah</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Electro dialysis reversal (EDR) performance for reject brine treatment of reverse osmosis desalination system</atitle><jtitle>PloS one</jtitle><date>2022-08-24</date><risdate>2022</risdate><volume>17</volume><issue>8</issue><spage>e0273240</spage><epage>e0273240</epage><pages>e0273240-e0273240</pages><issn>1932-6203</issn><eissn>1932-6203</eissn><abstract>In this study, the performance of bench-scale EDR was evaluated using the samples taken from the 1st and the 2nd stage RO from the Brackish Water Reverse Osmosis (BWRO) plant in Eshtehard, Iran. The measurements indicated that original TDS of the aquifer brackish water was equal to 3,229–3,664 mg/L, whereas TDS of the 1
st
stage RO brine was between 5,500 and 7,700 mg/L, that TDS of the 2
nd
stage RO brine was in the range of 9,500–10,600 mg/L. A batch bench-scale EDR system of 12 l/h was used with a direct electric current at three different scenarios. In the first, the brine was fed at 20°C (as a reference regulated point). In the second, temperature (14, 20, 26.5°C), and in the third, voltage were changed (6, 12, 18, 24 V) to investigate their influences on performance of the EDR process, while the other operational parameters (feed flow rate, recovery ratio, quality of feed brine)were kept constant. Based on the data analysis using the ANOVA and DUNCAN tests for the second and third scenarios, it was observed that the optimum TDS removal efficiency of the EDR process can be at temperature of 26.5°C and voltage of 18 V. On the other hand, the successful performance of the bench-scale EDR in reducing the 29,000 mg/L TDS and the 45,000 μmhos/cm EC of the 2
nd
stage brine to 1,716 mg/L (TDS) and 2,640 μmhos/cm (EC) (at 26.5°C and 24V) could be considered as the main achievement of this research. Overall, the hybrid process RO-EDR-RO can be considered as the best technical, environmental and economical scenario for the development of Eshtehard Desalination Plant phase 2 at full scale.</abstract><cop>San Francisco</cop><pub>Public Library of Science</pub><pmid>36001606</pmid><doi>10.1371/journal.pone.0273240</doi><orcidid>https://orcid.org/0000-0002-4973-318X</orcidid><oa>free_for_read</oa></addata></record> |
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| source | DOAJ Directory of Open Access Journals; Elektronische Zeitschriftenbibliothek - Frei zugängliche E-Journals; PubMed Central; Free Full-Text Journals in Chemistry; Public Library of Science (PLoS) |
| subjects | Aquatic resources Aquifers Brackish water Brines Cost recovery Data analysis Desalination Desalination plants Dialysis Drinking water Ecology and Environmental Sciences Electric currents Electric potential Electrodes Electrodialysis Engineering and Technology Evaluation Feed quality Flow velocity Freshwater resources Iran Management Membranes Performance evaluation Physical Sciences Research and Analysis Methods Reverse osmosis Saline water conversion plants Social Sciences Variance analysis Voltage |
| title | Electro dialysis reversal (EDR) performance for reject brine treatment of reverse osmosis desalination system |
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