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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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 |
work_keys_str_mv |
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