Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane

In this work, a loose reverse osmosis (RO) membrane (Osmonics AK model), capable of offering beforehand higher fluxes under lower operating pressure than typical tight reverse osmosis membranes but still offering similar rejection, was used for the final purification of olive mill wastewater. Howeve...

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Main Authors: J.M. Ochando-Pulido, M. Stoller, A. Martinez-Ferez
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2017-03-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/2260
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spelling doaj-d990a97c5a164aeaa71d309ef096077b2021-02-18T21:04:13ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162017-03-015710.3303/CET1757197Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis MembraneJ.M. Ochando-PulidoM. StollerA. Martinez-FerezIn this work, a loose reverse osmosis (RO) membrane (Osmonics AK model), capable of offering beforehand higher fluxes under lower operating pressure than typical tight reverse osmosis membranes but still offering similar rejection, was used for the final purification of olive mill wastewater. However, the output that a membrane may offer when it is virgin and readily used will change in time due to membrane fouling. If not properly considered, the advantages that a chosen membrane may offer in contrast with others would quickly and often irreversibly vanish, with the consequences in terms of capital expenses that this will represent. One approach to meet the investor’s needs to trust membrane technology is to guarantee that fouling will be inhibited as much as possible, but to overcome the loss of performance that fouling carries engineers overdesign the membrane plants by using too wide safety margins that trigger the costs sensibly. Since the mechanisms by which fouling phenomena are triggered are always complex, the osmotic-pressure resistances-in-series model can be a simple but reliable model to describe the membrane response and predict its performance in time. In this context, the normalized fouling measured on the examined RO membrane was found to be minimum in the operating pressure range between 5 and 8 bar (0.65-0.98, respectively), and it decreased down to 0.51 upon increasing the crossflow up to 5.09 m s-1, avoiding irreversible fouling. Moreover, significantly minor fouling (0.33) was attained at the lowest temperature, regularly experienced during the olive oil production campaign. On another hand, the rejection towards organic solutes was maintained above 97%. https://www.cetjournal.it/index.php/cet/article/view/2260
collection DOAJ
language English
format Article
sources DOAJ
author J.M. Ochando-Pulido
M. Stoller
A. Martinez-Ferez
spellingShingle J.M. Ochando-Pulido
M. Stoller
A. Martinez-Ferez
Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane
Chemical Engineering Transactions
author_facet J.M. Ochando-Pulido
M. Stoller
A. Martinez-Ferez
author_sort J.M. Ochando-Pulido
title Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane
title_short Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane
title_full Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane
title_fullStr Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane
title_full_unstemmed Analysis of Fouling Resistances under Dynamic Filtration of Pretreated Olive Mill Wastewater on a Loose Reverse Osmosis Membrane
title_sort analysis of fouling resistances under dynamic filtration of pretreated olive mill wastewater on a loose reverse osmosis membrane
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2017-03-01
description In this work, a loose reverse osmosis (RO) membrane (Osmonics AK model), capable of offering beforehand higher fluxes under lower operating pressure than typical tight reverse osmosis membranes but still offering similar rejection, was used for the final purification of olive mill wastewater. However, the output that a membrane may offer when it is virgin and readily used will change in time due to membrane fouling. If not properly considered, the advantages that a chosen membrane may offer in contrast with others would quickly and often irreversibly vanish, with the consequences in terms of capital expenses that this will represent. One approach to meet the investor’s needs to trust membrane technology is to guarantee that fouling will be inhibited as much as possible, but to overcome the loss of performance that fouling carries engineers overdesign the membrane plants by using too wide safety margins that trigger the costs sensibly. Since the mechanisms by which fouling phenomena are triggered are always complex, the osmotic-pressure resistances-in-series model can be a simple but reliable model to describe the membrane response and predict its performance in time. In this context, the normalized fouling measured on the examined RO membrane was found to be minimum in the operating pressure range between 5 and 8 bar (0.65-0.98, respectively), and it decreased down to 0.51 upon increasing the crossflow up to 5.09 m s-1, avoiding irreversible fouling. Moreover, significantly minor fouling (0.33) was attained at the lowest temperature, regularly experienced during the olive oil production campaign. On another hand, the rejection towards organic solutes was maintained above 97%.
url https://www.cetjournal.it/index.php/cet/article/view/2260
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