OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES

This study analyzed the effects of temperature and transmembrane pressure on the crossflow microfiltration process of arazá (Eugenia stipitata) juice treated with a commercial pectic enzyme preparation, thus finding the appropriate operation values of the process. Clarified arazá juice was obtained...

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Autores principales: Ángelo G. RAMÍREZ L., Diego F. de los RÍOS C., Carlos A. VÉLEZ P., Heidy L. GALLEGO O.
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Publicado: Universidad de Antioquia 2011
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spelling oai:doaj.org-article:7b1773cb85d04c17a842550d525f43e42021-11-19T04:13:47ZOPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES0121-40042145-2660https://doaj.org/article/7b1773cb85d04c17a842550d525f43e42011-09-01T00:00:00Zhttps://revistas.udea.edu.co/index.php/vitae/article/view/10071https://doaj.org/toc/0121-4004https://doaj.org/toc/2145-2660This study analyzed the effects of temperature and transmembrane pressure on the crossflow microfiltration process of arazá (Eugenia stipitata) juice treated with a commercial pectic enzyme preparation, thus finding the appropriate operation values of the process. Clarified arazá juice was obtained with a crossflow microfiltration pilot plant equipped with ceramic membranes with a 0.48 m2 total effective filtration area and mean pore diameter of 0.2 µm. The juice was evaluated at transmembrane pressures 1.5, 3.0 and 4.5 bar, and at temperatures of 30, 35 and 40ºC at different volumetric reduction factors. The tests were carried out using three systems (total recirculation, concentration, and continuous mode). In total recirculation, it was found that the most influential variable was the transmembrane pressures, and that the partial enzymatic liquefaction of the arazá juice, prior to microfiltration, produced an unusual pattern of permeate flux, characterized by an increase following an abrupt decrease at 4.5 bar and 6.5 m/s. In this case, the highest values of the flux were obtained when compared with those obtained during the crossflow microfiltration in concentration mode. After reaching the value of volumetric reduction factor (3.2), during the crossflow microfiltration in continuous mode, it was not necessary to stop the process as the volumetric reduction factor remained constant for the continuous removal of retained, achieving a high permeate flux in a short period of time 319 L/(h·m2), thus adding to the economic viability of the process.Ángelo G. RAMÍREZ L.Diego F. de los RÍOS C.Carlos A. VÉLEZ P.Heidy L. GALLEGO O.Universidad de AntioquiaarticleMicrofiltrationceramic membranesjuicesenzymatic liquefactionvolumetric reduction factors.Food processing and manufactureTP368-456Pharmaceutical industryHD9665-9675ENVitae, Vol 18, Iss 2 (2011)
institution DOAJ
collection DOAJ
language EN
topic Microfiltration
ceramic membranes
juices
enzymatic liquefaction
volumetric reduction factors.
Food processing and manufacture
TP368-456
Pharmaceutical industry
HD9665-9675
spellingShingle Microfiltration
ceramic membranes
juices
enzymatic liquefaction
volumetric reduction factors.
Food processing and manufacture
TP368-456
Pharmaceutical industry
HD9665-9675
Ángelo G. RAMÍREZ L.
Diego F. de los RÍOS C.
Carlos A. VÉLEZ P.
Heidy L. GALLEGO O.
OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES
description This study analyzed the effects of temperature and transmembrane pressure on the crossflow microfiltration process of arazá (Eugenia stipitata) juice treated with a commercial pectic enzyme preparation, thus finding the appropriate operation values of the process. Clarified arazá juice was obtained with a crossflow microfiltration pilot plant equipped with ceramic membranes with a 0.48 m2 total effective filtration area and mean pore diameter of 0.2 µm. The juice was evaluated at transmembrane pressures 1.5, 3.0 and 4.5 bar, and at temperatures of 30, 35 and 40ºC at different volumetric reduction factors. The tests were carried out using three systems (total recirculation, concentration, and continuous mode). In total recirculation, it was found that the most influential variable was the transmembrane pressures, and that the partial enzymatic liquefaction of the arazá juice, prior to microfiltration, produced an unusual pattern of permeate flux, characterized by an increase following an abrupt decrease at 4.5 bar and 6.5 m/s. In this case, the highest values of the flux were obtained when compared with those obtained during the crossflow microfiltration in concentration mode. After reaching the value of volumetric reduction factor (3.2), during the crossflow microfiltration in continuous mode, it was not necessary to stop the process as the volumetric reduction factor remained constant for the continuous removal of retained, achieving a high permeate flux in a short period of time 319 L/(h·m2), thus adding to the economic viability of the process.
format article
author Ángelo G. RAMÍREZ L.
Diego F. de los RÍOS C.
Carlos A. VÉLEZ P.
Heidy L. GALLEGO O.
author_facet Ángelo G. RAMÍREZ L.
Diego F. de los RÍOS C.
Carlos A. VÉLEZ P.
Heidy L. GALLEGO O.
author_sort Ángelo G. RAMÍREZ L.
title OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES
title_short OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES
title_full OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES
title_fullStr OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES
title_full_unstemmed OPTIMIZATION OF THE CROSSFLOW MICROFILTRATION OF ARAZÁ JUICE (<I>Eugenia stipitata</I>) UNDER DIFFERENT OPERATION MODES
title_sort optimization of the crossflow microfiltration of arazá juice (<i>eugenia stipitata</i>) under different operation modes
publisher Universidad de Antioquia
publishDate 2011
url https://doaj.org/article/7b1773cb85d04c17a842550d525f43e4
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