Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane

The aim of this work was the study on the separation of soybean oil/n-butane mixtures using a commercial hollow fiber ultrafiltration membrane (50 kDa). Oil/n-butane mixtures with mass ratios of 1:1 and 1:3 (wt), with the feed pressures of 5, 7 and 10 bar and transmembrane pressure of 1 bar were stu...

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Main Authors: M. V. Tres, J. C. Racoski, R. Nobrega, R. B. Carvalho, J. V. Oliveira, M. Di Luccio
Format: Article
Language:English
Published: Brazilian Society of Chemical Engineering 2014-03-01
Series:Brazilian Journal of Chemical Engineering
Subjects:
Online Access:http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322014000100022&lng=en&tlng=en
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spelling doaj-8430643871b84fc58399fa59b2b0def52020-11-25T01:24:47ZengBrazilian Society of Chemical EngineeringBrazilian Journal of Chemical Engineering0104-66322014-03-0131124324910.1590/S0104-66322014000100022S0104-66322014000100022Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membraneM. V. Tres0J. C. Racoski1R. Nobrega2R. B. Carvalho3J. V. Oliveira4M. Di Luccio5Universidade Regional Integrada do Alto do Uruguai e das MissõesUniversidade Regional Integrada do Alto do Uruguai e das MissõesParque Tecnológico do Rio de JaneiroParque Tecnológico do Rio de JaneiroUniversidade Federal de Santa CatarinaUniversidade Federal de Santa CatarinaThe aim of this work was the study on the separation of soybean oil/n-butane mixtures using a commercial hollow fiber ultrafiltration membrane (50 kDa). Oil/n-butane mixtures with mass ratios of 1:1 and 1:3 (wt), with the feed pressures of 5, 7 and 10 bar and transmembrane pressure of 1 bar were studied. Rejections of oil between 21 to 97.2%, oil fluxes between 0.04 and 0.98 kg/m² h and n-butane fluxes between 4 and 46 kg/m² h were observed, strongly influenced by the feed concentration. The increase in oil/n-butane mass ratio caused an increase in oil rejection and a decrease in the permeate flux of oil for most assays. The increase in the operating pressure caused an increase in oil flux and a consequent decrease in oil rejection. No degradation was observed in the membrane module during the operation with this non-aqueous feed stream, as confirmed by integrity tests.http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322014000100022&lng=en&tlng=enSoybean oiln-butaneSolvent recoveryHollow fiberMembrane conditioning
collection DOAJ
language English
format Article
sources DOAJ
author M. V. Tres
J. C. Racoski
R. Nobrega
R. B. Carvalho
J. V. Oliveira
M. Di Luccio
spellingShingle M. V. Tres
J. C. Racoski
R. Nobrega
R. B. Carvalho
J. V. Oliveira
M. Di Luccio
Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
Brazilian Journal of Chemical Engineering
Soybean oil
n-butane
Solvent recovery
Hollow fiber
Membrane conditioning
author_facet M. V. Tres
J. C. Racoski
R. Nobrega
R. B. Carvalho
J. V. Oliveira
M. Di Luccio
author_sort M. V. Tres
title Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
title_short Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
title_full Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
title_fullStr Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
title_full_unstemmed Solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
title_sort solvent recovery from soybean oil/n-butane mixtures using a hollow fiber ultrafiltration membrane
publisher Brazilian Society of Chemical Engineering
series Brazilian Journal of Chemical Engineering
issn 0104-6632
publishDate 2014-03-01
description The aim of this work was the study on the separation of soybean oil/n-butane mixtures using a commercial hollow fiber ultrafiltration membrane (50 kDa). Oil/n-butane mixtures with mass ratios of 1:1 and 1:3 (wt), with the feed pressures of 5, 7 and 10 bar and transmembrane pressure of 1 bar were studied. Rejections of oil between 21 to 97.2%, oil fluxes between 0.04 and 0.98 kg/m² h and n-butane fluxes between 4 and 46 kg/m² h were observed, strongly influenced by the feed concentration. The increase in oil/n-butane mass ratio caused an increase in oil rejection and a decrease in the permeate flux of oil for most assays. The increase in the operating pressure caused an increase in oil flux and a consequent decrease in oil rejection. No degradation was observed in the membrane module during the operation with this non-aqueous feed stream, as confirmed by integrity tests.
topic Soybean oil
n-butane
Solvent recovery
Hollow fiber
Membrane conditioning
url http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322014000100022&lng=en&tlng=en
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AT rbcarvalho solventrecoveryfromsoybeanoilnbutanemixturesusingahollowfiberultrafiltrationmembrane
AT jvoliveira solventrecoveryfromsoybeanoilnbutanemixturesusingahollowfiberultrafiltrationmembrane
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