Modeling the supercritical desorption of orange essential oil from a silica-gel bed

One of the most important byproducts of the orange juice industry is the oil phase. This is a mixture of terpenes, alcohols, and aldehydes, dissolved in approximately 96% limonene. To satisfactorily use oil phase as an ingredient in the food and cosmetics industries separation of the limonene is req...

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Main Authors: Silva E.A., Cardozo-Filho L., Wolff F., Meireles M.A.A.
Format: Article
Language:English
Published: Brazilian Society of Chemical Engineering 2000-01-01
Series:Brazilian Journal of Chemical Engineering
Subjects:
Online Access:http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300004
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spelling doaj-387a8e27f87b4c1794f3eb830cf735102020-11-24T22:51:34ZengBrazilian Society of Chemical EngineeringBrazilian Journal of Chemical Engineering0104-66321678-43832000-01-01173283296Modeling the supercritical desorption of orange essential oil from a silica-gel bedSilva E.A.Cardozo-Filho L.Wolff F.Meireles M.A.A.One of the most important byproducts of the orange juice industry is the oil phase. This is a mixture of terpenes, alcohols, and aldehydes, dissolved in approximately 96% limonene. To satisfactorily use oil phase as an ingredient in the food and cosmetics industries separation of the limonene is required. One possibility is to use a fixed bed of silica gel to remove the light or aroma compounds from the limonene. The aroma substances are then extracted from the bed of silica gel using supercritical carbon dioxide. This work deals with the modeling of the desorption step of the process using mass balance equations coupled with the Langmuir equilibrium isotherm. Data taken from the literature for the overall extraction curves were used together with empirical correlations to calculate the concentration profile of solute in the supercritical phase at the bed outlet. The system of equations was solved by the finite volume technique. The overall extraction curves calculated were in good agreement with the experimental ones.http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300004orange oiloil phasedesorptionsupercritical fluidsmass transfer modelingsolid matricescarbon dioxide
collection DOAJ
language English
format Article
sources DOAJ
author Silva E.A.
Cardozo-Filho L.
Wolff F.
Meireles M.A.A.
spellingShingle Silva E.A.
Cardozo-Filho L.
Wolff F.
Meireles M.A.A.
Modeling the supercritical desorption of orange essential oil from a silica-gel bed
Brazilian Journal of Chemical Engineering
orange oil
oil phase
desorption
supercritical fluids
mass transfer modeling
solid matrices
carbon dioxide
author_facet Silva E.A.
Cardozo-Filho L.
Wolff F.
Meireles M.A.A.
author_sort Silva E.A.
title Modeling the supercritical desorption of orange essential oil from a silica-gel bed
title_short Modeling the supercritical desorption of orange essential oil from a silica-gel bed
title_full Modeling the supercritical desorption of orange essential oil from a silica-gel bed
title_fullStr Modeling the supercritical desorption of orange essential oil from a silica-gel bed
title_full_unstemmed Modeling the supercritical desorption of orange essential oil from a silica-gel bed
title_sort modeling the supercritical desorption of orange essential oil from a silica-gel bed
publisher Brazilian Society of Chemical Engineering
series Brazilian Journal of Chemical Engineering
issn 0104-6632
1678-4383
publishDate 2000-01-01
description One of the most important byproducts of the orange juice industry is the oil phase. This is a mixture of terpenes, alcohols, and aldehydes, dissolved in approximately 96% limonene. To satisfactorily use oil phase as an ingredient in the food and cosmetics industries separation of the limonene is required. One possibility is to use a fixed bed of silica gel to remove the light or aroma compounds from the limonene. The aroma substances are then extracted from the bed of silica gel using supercritical carbon dioxide. This work deals with the modeling of the desorption step of the process using mass balance equations coupled with the Langmuir equilibrium isotherm. Data taken from the literature for the overall extraction curves were used together with empirical correlations to calculate the concentration profile of solute in the supercritical phase at the bed outlet. The system of equations was solved by the finite volume technique. The overall extraction curves calculated were in good agreement with the experimental ones.
topic orange oil
oil phase
desorption
supercritical fluids
mass transfer modeling
solid matrices
carbon dioxide
url http://www.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300004
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