Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes

The fractionation of a protein hydrolysate obtained from tuna processing by-products by means of a membrane cascade integrating ultrafiltration (UF) and nanofiltration (NF) membranes was proposed in order to separate and purify the protein fraction between 1 and 4 kDa, which is the most interesting...

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Main Authors: R. Abejón, A. Abejón, M.-P. Belleville, A. Garea, A. Irabien, J. Sanchez-Marcano
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2016-08-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/3694
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spelling doaj-88fdaae5291e4493a91ae1edc7f4f2fe2021-02-19T21:06:15ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162016-08-015210.3303/CET1652048Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration MembranesR. AbejónA. AbejónM.-P. BellevilleA. GareaA. IrabienJ. Sanchez-MarcanoThe fractionation of a protein hydrolysate obtained from tuna processing by-products by means of a membrane cascade integrating ultrafiltration (UF) and nanofiltration (NF) membranes was proposed in order to separate and purify the protein fraction between 1 and 4 kDa, which is the most interesting for nutraceutical purposes. A simulation model, based on mass balances and empirical equations for describing permeate flux and rejection of protein fractions, was developed and complemented with a simple cost estimation model. The product purity (49.3 %) and the process yield (62.6 %) were independent of the total water consumption of the process, but high water consumptions were required to maintain the total protein content of the stream below upper bounds that assured the absence of membrane clogging. The implementation of a water recovery system, based on an additional tight NF stage, implied improvements in both environmental and economic aspects of the process.https://www.cetjournal.it/index.php/cet/article/view/3694
collection DOAJ
language English
format Article
sources DOAJ
author R. Abejón
A. Abejón
M.-P. Belleville
A. Garea
A. Irabien
J. Sanchez-Marcano
spellingShingle R. Abejón
A. Abejón
M.-P. Belleville
A. Garea
A. Irabien
J. Sanchez-Marcano
Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes
Chemical Engineering Transactions
author_facet R. Abejón
A. Abejón
M.-P. Belleville
A. Garea
A. Irabien
J. Sanchez-Marcano
author_sort R. Abejón
title Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes
title_short Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes
title_full Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes
title_fullStr Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes
title_full_unstemmed Water Recovery and Reuse in the Fractionation of Protein Hydrolysate by Ultrafiltration and Nanofiltration Membranes
title_sort water recovery and reuse in the fractionation of protein hydrolysate by ultrafiltration and nanofiltration membranes
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2016-08-01
description The fractionation of a protein hydrolysate obtained from tuna processing by-products by means of a membrane cascade integrating ultrafiltration (UF) and nanofiltration (NF) membranes was proposed in order to separate and purify the protein fraction between 1 and 4 kDa, which is the most interesting for nutraceutical purposes. A simulation model, based on mass balances and empirical equations for describing permeate flux and rejection of protein fractions, was developed and complemented with a simple cost estimation model. The product purity (49.3 %) and the process yield (62.6 %) were independent of the total water consumption of the process, but high water consumptions were required to maintain the total protein content of the stream below upper bounds that assured the absence of membrane clogging. The implementation of a water recovery system, based on an additional tight NF stage, implied improvements in both environmental and economic aspects of the process.
url https://www.cetjournal.it/index.php/cet/article/view/3694
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