Cargando…
Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile
As world demand for clean water increases, reverse osmosis (RO) desalination has emerged as an attractive solution. Continuous RO is the most used desalination technology today. However, a new generation of configurations, working in unsteady-state feed concentration and pressure, have gained more a...
Autores principales: | , , , , , |
---|---|
Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2021
|
Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7997241/ https://www.ncbi.nlm.nih.gov/pubmed/33671027 http://dx.doi.org/10.3390/membranes11030173 |
_version_ | 1783670283584929792 |
---|---|
author | Chougradi, Abdeljalil Zaviska, François Abed, Ahmed Harmand, Jérôme Jellal, Jamal-Eddine Heran, Marc |
author_facet | Chougradi, Abdeljalil Zaviska, François Abed, Ahmed Harmand, Jérôme Jellal, Jamal-Eddine Heran, Marc |
author_sort | Chougradi, Abdeljalil |
collection | PubMed |
description | As world demand for clean water increases, reverse osmosis (RO) desalination has emerged as an attractive solution. Continuous RO is the most used desalination technology today. However, a new generation of configurations, working in unsteady-state feed concentration and pressure, have gained more attention recently, including the batch RO process. Our work presents a mathematical modeling for batch RO that offers the possibility of monitoring all variables of the process, including specific energy consumption, as a function of time and the recovery ratio. Validation is achieved by comparison with data from the experimental set-up and an existing model in the literature. Energetic comparison with continuous RO processes confirms that batch RO can be more energy efficient than can continuous RO, especially at a higher recovery ratio. It used, at recovery, 31% less energy for seawater and 19% less energy for brackish water. Modeling also proves that the batch RO process does not have to function under constant flux to deliver good energetic performance. In fact, under a linear pressure profile, batch RO can still deliver better energetic performance than can a continuous configuration. The parameters analysis shows that salinity, pump and energy recovery devices efficiencies are directly linked to the energy demand. While increasing feed volume has a limited effect after a certain volume due to dilution, it also shows, interestingly, a recovery ratio interval in which feed volume does not affect specific energy consumption. |
format | Online Article Text |
id | pubmed-7997241 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2021 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-79972412021-03-27 Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile Chougradi, Abdeljalil Zaviska, François Abed, Ahmed Harmand, Jérôme Jellal, Jamal-Eddine Heran, Marc Membranes (Basel) Article As world demand for clean water increases, reverse osmosis (RO) desalination has emerged as an attractive solution. Continuous RO is the most used desalination technology today. However, a new generation of configurations, working in unsteady-state feed concentration and pressure, have gained more attention recently, including the batch RO process. Our work presents a mathematical modeling for batch RO that offers the possibility of monitoring all variables of the process, including specific energy consumption, as a function of time and the recovery ratio. Validation is achieved by comparison with data from the experimental set-up and an existing model in the literature. Energetic comparison with continuous RO processes confirms that batch RO can be more energy efficient than can continuous RO, especially at a higher recovery ratio. It used, at recovery, 31% less energy for seawater and 19% less energy for brackish water. Modeling also proves that the batch RO process does not have to function under constant flux to deliver good energetic performance. In fact, under a linear pressure profile, batch RO can still deliver better energetic performance than can a continuous configuration. The parameters analysis shows that salinity, pump and energy recovery devices efficiencies are directly linked to the energy demand. While increasing feed volume has a limited effect after a certain volume due to dilution, it also shows, interestingly, a recovery ratio interval in which feed volume does not affect specific energy consumption. MDPI 2021-02-28 /pmc/articles/PMC7997241/ /pubmed/33671027 http://dx.doi.org/10.3390/membranes11030173 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 (http://creativecommons.org/licenses/by/4.0/ (https://creativecommons.org/licenses/by/4.0/) ). |
spellingShingle | Article Chougradi, Abdeljalil Zaviska, François Abed, Ahmed Harmand, Jérôme Jellal, Jamal-Eddine Heran, Marc Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile |
title | Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile |
title_full | Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile |
title_fullStr | Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile |
title_full_unstemmed | Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile |
title_short | Batch Reverse Osmosis Desalination Modeling under a Time-Dependent Pressure Profile |
title_sort | batch reverse osmosis desalination modeling under a time-dependent pressure profile |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7997241/ https://www.ncbi.nlm.nih.gov/pubmed/33671027 http://dx.doi.org/10.3390/membranes11030173 |
work_keys_str_mv | AT chougradiabdeljalil batchreverseosmosisdesalinationmodelingunderatimedependentpressureprofile AT zaviskafrancois batchreverseosmosisdesalinationmodelingunderatimedependentpressureprofile AT abedahmed batchreverseosmosisdesalinationmodelingunderatimedependentpressureprofile AT harmandjerome batchreverseosmosisdesalinationmodelingunderatimedependentpressureprofile AT jellaljamaleddine batchreverseosmosisdesalinationmodelingunderatimedependentpressureprofile AT heranmarc batchreverseosmosisdesalinationmodelingunderatimedependentpressureprofile |