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Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater
A secondary treatment for olive mill wastewater coming from factories working with the two-phase olive oil production process (OMW-2) has been set-up on an industrial scale in an olive oil mill in the premises of Jaén (Spain). The secondary treatment comprises Fenton-like oxidation followed by flocc...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
MDPI
2013
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4021955/ https://www.ncbi.nlm.nih.gov/pubmed/24957058 http://dx.doi.org/10.3390/membranes3040285 |
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author | Ochando-Pulido, Javier Miguel Hodaifa, Gassan Victor-Ortega, Maria Dolores Martinez-Ferez, Antonio |
author_facet | Ochando-Pulido, Javier Miguel Hodaifa, Gassan Victor-Ortega, Maria Dolores Martinez-Ferez, Antonio |
author_sort | Ochando-Pulido, Javier Miguel |
collection | PubMed |
description | A secondary treatment for olive mill wastewater coming from factories working with the two-phase olive oil production process (OMW-2) has been set-up on an industrial scale in an olive oil mill in the premises of Jaén (Spain). The secondary treatment comprises Fenton-like oxidation followed by flocculation-sedimentation and filtration through olive stones. In this work, performance modelization and preliminary cost analysis of a final reverse osmosis (RO) process was examined on pilot scale for ulterior purification of OMW-2 with the goal of closing the loop of the industrial production process. Reduction of concentration polarization on the RO membrane equal to 26.3% was provided upon increment of the turbulence over the membrane to values of Reynolds number equal to 2.6 × 10(4). Medium operating pressure (25 bar) should be chosen to achieve significant steady state permeate flux (21.1 L h(−1) m(−2)) and minimize membrane fouling, ensuring less than 14.7% flux drop and up to 90% feed recovery. Under these conditions, irreversible fouling below 0.08 L h(−)(2) m(−)(2) bar(−)(1) helped increase the longevity of the membrane and reduce the costs of the treatment. For 10 m(3) day(−1) OMW-2 on average, 47.4 m(2) required membrane area and 0.87 € m(−3) total costs for the RO process were estimated. |
format | Online Article Text |
id | pubmed-4021955 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2013 |
publisher | MDPI |
record_format | MEDLINE/PubMed |
spelling | pubmed-40219552014-05-27 Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater Ochando-Pulido, Javier Miguel Hodaifa, Gassan Victor-Ortega, Maria Dolores Martinez-Ferez, Antonio Membranes (Basel) Article A secondary treatment for olive mill wastewater coming from factories working with the two-phase olive oil production process (OMW-2) has been set-up on an industrial scale in an olive oil mill in the premises of Jaén (Spain). The secondary treatment comprises Fenton-like oxidation followed by flocculation-sedimentation and filtration through olive stones. In this work, performance modelization and preliminary cost analysis of a final reverse osmosis (RO) process was examined on pilot scale for ulterior purification of OMW-2 with the goal of closing the loop of the industrial production process. Reduction of concentration polarization on the RO membrane equal to 26.3% was provided upon increment of the turbulence over the membrane to values of Reynolds number equal to 2.6 × 10(4). Medium operating pressure (25 bar) should be chosen to achieve significant steady state permeate flux (21.1 L h(−1) m(−2)) and minimize membrane fouling, ensuring less than 14.7% flux drop and up to 90% feed recovery. Under these conditions, irreversible fouling below 0.08 L h(−)(2) m(−)(2) bar(−)(1) helped increase the longevity of the membrane and reduce the costs of the treatment. For 10 m(3) day(−1) OMW-2 on average, 47.4 m(2) required membrane area and 0.87 € m(−3) total costs for the RO process were estimated. MDPI 2013-10-11 /pmc/articles/PMC4021955/ /pubmed/24957058 http://dx.doi.org/10.3390/membranes3040285 Text en © 2013 by the authors; licensee MDPI, Basel, Switzerland. http://creativecommons.org/licenses/by/3.0/ This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution license (http://creativecommons.org/licenses/by/3.0/). |
spellingShingle | Article Ochando-Pulido, Javier Miguel Hodaifa, Gassan Victor-Ortega, Maria Dolores Martinez-Ferez, Antonio Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater |
title | Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater |
title_full | Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater |
title_fullStr | Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater |
title_full_unstemmed | Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater |
title_short | Performance Modeling and Cost Analysis of a Pilot-Scale Reverse Osmosis Process for the Final Purification of Olive Mill Wastewater |
title_sort | performance modeling and cost analysis of a pilot-scale reverse osmosis process for the final purification of olive mill wastewater |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4021955/ https://www.ncbi.nlm.nih.gov/pubmed/24957058 http://dx.doi.org/10.3390/membranes3040285 |
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