Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol

Detalhes bibliográficos
Autor(a) principal: Pasquel,A.
Data de Publicação: 2000
Outros Autores: Meireles,M.A.A., Marques,M.O.M., Petenate,A.J.
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Brazilian Journal of Chemical Engineering
Texto Completo: http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300003
Resumo: Stevia leaves are an important source of natural sugar substitute. There are some restrictions on the use of stevia extract because of its distinctive aftertaste. Some authors attribute this to soluble material other than the stevia glycosides, even though it is well known that stevia glycosides have to some extent a bitter taste. Therefore, the purpose of this work was to develop a process to obtain stevia extract of a better quality. The proposed process includes two steps: i) Pretreatment of the leaves by SCFE; ii) Extraction of the stevia glycosides by SCFE using CO2 as solvent and water and/or ethanol as cosolvent. The mean total yield for SCFE pretreatment was 3.0%. The yields for SCFE with cosolvent of stevia glycosides were below 0.50%, except at 120 bar, 16°C, and 9.5% (molar) of water. Under this condition, total yield was 3.4%. The quality of the glycosidic fraction with respect to its capacity as sweetener was better for the SCFE extract as compared to extract obtained by the conventional process. The overall extraction curves were well described by the Lack extended model.
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spelling Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanolsteviasupercritical extractionmass transfersteviosiderebaudioside-AglycosidecosolventwaterethanolStevia leaves are an important source of natural sugar substitute. There are some restrictions on the use of stevia extract because of its distinctive aftertaste. Some authors attribute this to soluble material other than the stevia glycosides, even though it is well known that stevia glycosides have to some extent a bitter taste. Therefore, the purpose of this work was to develop a process to obtain stevia extract of a better quality. The proposed process includes two steps: i) Pretreatment of the leaves by SCFE; ii) Extraction of the stevia glycosides by SCFE using CO2 as solvent and water and/or ethanol as cosolvent. The mean total yield for SCFE pretreatment was 3.0%. The yields for SCFE with cosolvent of stevia glycosides were below 0.50%, except at 120 bar, 16°C, and 9.5% (molar) of water. Under this condition, total yield was 3.4%. The quality of the glycosidic fraction with respect to its capacity as sweetener was better for the SCFE extract as compared to extract obtained by the conventional process. The overall extraction curves were well described by the Lack extended model.Brazilian Society of Chemical Engineering2000-09-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300003Brazilian Journal of Chemical Engineering v.17 n.3 2000reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322000000300003info:eu-repo/semantics/openAccessPasquel,A.Meireles,M.A.A.Marques,M.O.M.Petenate,A.J.eng2000-10-18T00:00:00Zoai:scielo:S0104-66322000000300003Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2000-10-18T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
title Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
spellingShingle Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
Pasquel,A.
stevia
supercritical extraction
mass transfer
stevioside
rebaudioside-A
glycoside
cosolvent
water
ethanol
title_short Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
title_full Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
title_fullStr Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
title_full_unstemmed Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
title_sort Extraction of stevia glycosides with CO2 + water, CO2 + ethanol, and CO2 + water + ethanol
author Pasquel,A.
author_facet Pasquel,A.
Meireles,M.A.A.
Marques,M.O.M.
Petenate,A.J.
author_role author
author2 Meireles,M.A.A.
Marques,M.O.M.
Petenate,A.J.
author2_role author
author
author
dc.contributor.author.fl_str_mv Pasquel,A.
Meireles,M.A.A.
Marques,M.O.M.
Petenate,A.J.
dc.subject.por.fl_str_mv stevia
supercritical extraction
mass transfer
stevioside
rebaudioside-A
glycoside
cosolvent
water
ethanol
topic stevia
supercritical extraction
mass transfer
stevioside
rebaudioside-A
glycoside
cosolvent
water
ethanol
description Stevia leaves are an important source of natural sugar substitute. There are some restrictions on the use of stevia extract because of its distinctive aftertaste. Some authors attribute this to soluble material other than the stevia glycosides, even though it is well known that stevia glycosides have to some extent a bitter taste. Therefore, the purpose of this work was to develop a process to obtain stevia extract of a better quality. The proposed process includes two steps: i) Pretreatment of the leaves by SCFE; ii) Extraction of the stevia glycosides by SCFE using CO2 as solvent and water and/or ethanol as cosolvent. The mean total yield for SCFE pretreatment was 3.0%. The yields for SCFE with cosolvent of stevia glycosides were below 0.50%, except at 120 bar, 16°C, and 9.5% (molar) of water. Under this condition, total yield was 3.4%. The quality of the glycosidic fraction with respect to its capacity as sweetener was better for the SCFE extract as compared to extract obtained by the conventional process. The overall extraction curves were well described by the Lack extended model.
publishDate 2000
dc.date.none.fl_str_mv 2000-09-01
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300003
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322000000300003
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/S0104-66322000000300003
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv text/html
dc.publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
dc.source.none.fl_str_mv Brazilian Journal of Chemical Engineering v.17 n.3 2000
reponame:Brazilian Journal of Chemical Engineering
instname:Associação Brasileira de Engenharia Química (ABEQ)
instacron:ABEQ
instname_str Associação Brasileira de Engenharia Química (ABEQ)
instacron_str ABEQ
institution ABEQ
reponame_str Brazilian Journal of Chemical Engineering
collection Brazilian Journal of Chemical Engineering
repository.name.fl_str_mv Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)
repository.mail.fl_str_mv rgiudici@usp.br||rgiudici@usp.br
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