Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis

Detalhes bibliográficos
Autor(a) principal: Courtial, Camila Gambini Pereira
Data de Publicação: 2007
Outros Autores: Rosa, Paulo de Tarso Vieira e, Meireles, Maria Angela de Almeida
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UFRN
Texto Completo: https://repositorio.ufrn.br/handle/123456789/32548
Resumo: In the present work, the technical and economical analysis of extraction and isolation of indole alkaloids from Tabernaemontana catharinensis is presented. The extraction was carried out using supercritical CO2 as solvent and ethanol as cosolvent (5%, v/v). The global yield isotherms were determined at 35 and 45 ◦C for pressures of 150–350 bar. The mass transfer rate for the constant extraction rate period (CER), the duration of the CER period, and the mass ratio of solute in the fluid phase at the bed outlet were calculated. The extraction curves were adjusted by Crank, Goto et al. and Esqu´ıvel et al. models. The economical analysis was carried out considering that the cost of manufacturing can be obtained in terms of the costs of investment, operational labor, raw material, waste treatment and utilities. The higher global yields were obtained at 350 bar (1.30×10−2 and 1.54×10−2 kg/kg, at temperatures of 35 and 45 ◦C, respectively). The Goto’s model was able to quantitatively describe the experimental data. The cost of manufacturing the extracts obtained at 350 bar, 45 ◦C, using 5% (v/v) of ethanol was US$ 79.35 kg−1 of extract. Using previous experimental data obtained at 300 bar, 55 ◦C, using 10% of ethanol (v/v), the cost of manufacturing for the fractionation process to obtain a rich alkaloidal fraction (AF) was US$ 440.31 kg−1 of alkaloids
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spelling Courtial, Camila Gambini PereiraRosa, Paulo de Tarso Vieira eMeireles, Maria Angela de Almeida2021-05-21T19:01:02Z2021-05-21T19:01:02Z2007-03PEREIRA, C. G.; ROSA, P.T.V. ; MEIRELES, M.A.A. . Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC.: Technical and economical analysis. The Journal of Supercritical Fluids, v. 40, p. 232-238, 2007. Disponível em: https://www.sciencedirect.com/science/article/abs/pii/S0896844606001641?via%3Dihub. Acesso em: 08 abr. 2021. https://doi.org/10.1016/j.supflu.2006.07.0010896-8446https://repositorio.ufrn.br/handle/123456789/3254810.1016/j.supflu.2006.07.001ElsevierAttribution 3.0 Brazilhttp://creativecommons.org/licenses/by/3.0/br/info:eu-repo/semantics/openAccessIndole alkaloidsLeishmaniasisSupercritical fluid extractionTabernaemontana catharinensisTechnical and economical analysisExtraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysisinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleIn the present work, the technical and economical analysis of extraction and isolation of indole alkaloids from Tabernaemontana catharinensis is presented. The extraction was carried out using supercritical CO2 as solvent and ethanol as cosolvent (5%, v/v). The global yield isotherms were determined at 35 and 45 ◦C for pressures of 150–350 bar. The mass transfer rate for the constant extraction rate period (CER), the duration of the CER period, and the mass ratio of solute in the fluid phase at the bed outlet were calculated. The extraction curves were adjusted by Crank, Goto et al. and Esqu´ıvel et al. models. The economical analysis was carried out considering that the cost of manufacturing can be obtained in terms of the costs of investment, operational labor, raw material, waste treatment and utilities. The higher global yields were obtained at 350 bar (1.30×10−2 and 1.54×10−2 kg/kg, at temperatures of 35 and 45 ◦C, respectively). The Goto’s model was able to quantitatively describe the experimental data. The cost of manufacturing the extracts obtained at 350 bar, 45 ◦C, using 5% (v/v) of ethanol was US$ 79.35 kg−1 of extract. Using previous experimental data obtained at 300 bar, 55 ◦C, using 10% of ethanol (v/v), the cost of manufacturing for the fractionation process to obtain a rich alkaloidal fraction (AF) was US$ 440.31 kg−1 of alkaloidsengreponame:Repositório Institucional da UFRNinstname:Universidade Federal do Rio Grande do Norte (UFRN)instacron:UFRNORIGINALExtractionAndIsolation_PEREIRA_2007.pdfExtractionAndIsolation_PEREIRA_2007.pdfArtigoapplication/pdf379590https://repositorio.ufrn.br/bitstream/123456789/32548/1/ExtractionAndIsolation_PEREIRA_2007.pdff161dfd5ed3ccb310c153ff4b49d94c9MD51CC-LICENSElicense_rdflicense_rdfapplication/rdf+xml; charset=utf-8914https://repositorio.ufrn.br/bitstream/123456789/32548/2/license_rdf4d2950bda3d176f570a9f8b328dfbbefMD52LICENSElicense.txtlicense.txttext/plain; charset=utf-81484https://repositorio.ufrn.br/bitstream/123456789/32548/3/license.txte9597aa2854d128fd968be5edc8a28d9MD53123456789/325482021-05-21 16:01:03.851oai:https://repositorio.ufrn.br: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Repositório de PublicaçõesPUBhttp://repositorio.ufrn.br/oai/opendoar:2021-05-21T19:01:03Repositório Institucional da UFRN - Universidade Federal do Rio Grande do Norte (UFRN)false
dc.title.pt_BR.fl_str_mv Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
title Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
spellingShingle Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
Courtial, Camila Gambini Pereira
Indole alkaloids
Leishmaniasis
Supercritical fluid extraction
Tabernaemontana catharinensis
Technical and economical analysis
title_short Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
title_full Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
title_fullStr Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
title_full_unstemmed Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
title_sort Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC: technical and economical analysis
author Courtial, Camila Gambini Pereira
author_facet Courtial, Camila Gambini Pereira
Rosa, Paulo de Tarso Vieira e
Meireles, Maria Angela de Almeida
author_role author
author2 Rosa, Paulo de Tarso Vieira e
Meireles, Maria Angela de Almeida
author2_role author
author
dc.contributor.author.fl_str_mv Courtial, Camila Gambini Pereira
Rosa, Paulo de Tarso Vieira e
Meireles, Maria Angela de Almeida
dc.subject.por.fl_str_mv Indole alkaloids
Leishmaniasis
Supercritical fluid extraction
Tabernaemontana catharinensis
Technical and economical analysis
topic Indole alkaloids
Leishmaniasis
Supercritical fluid extraction
Tabernaemontana catharinensis
Technical and economical analysis
description In the present work, the technical and economical analysis of extraction and isolation of indole alkaloids from Tabernaemontana catharinensis is presented. The extraction was carried out using supercritical CO2 as solvent and ethanol as cosolvent (5%, v/v). The global yield isotherms were determined at 35 and 45 ◦C for pressures of 150–350 bar. The mass transfer rate for the constant extraction rate period (CER), the duration of the CER period, and the mass ratio of solute in the fluid phase at the bed outlet were calculated. The extraction curves were adjusted by Crank, Goto et al. and Esqu´ıvel et al. models. The economical analysis was carried out considering that the cost of manufacturing can be obtained in terms of the costs of investment, operational labor, raw material, waste treatment and utilities. The higher global yields were obtained at 350 bar (1.30×10−2 and 1.54×10−2 kg/kg, at temperatures of 35 and 45 ◦C, respectively). The Goto’s model was able to quantitatively describe the experimental data. The cost of manufacturing the extracts obtained at 350 bar, 45 ◦C, using 5% (v/v) of ethanol was US$ 79.35 kg−1 of extract. Using previous experimental data obtained at 300 bar, 55 ◦C, using 10% of ethanol (v/v), the cost of manufacturing for the fractionation process to obtain a rich alkaloidal fraction (AF) was US$ 440.31 kg−1 of alkaloids
publishDate 2007
dc.date.issued.fl_str_mv 2007-03
dc.date.accessioned.fl_str_mv 2021-05-21T19:01:02Z
dc.date.available.fl_str_mv 2021-05-21T19:01:02Z
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dc.identifier.citation.fl_str_mv PEREIRA, C. G.; ROSA, P.T.V. ; MEIRELES, M.A.A. . Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC.: Technical and economical analysis. The Journal of Supercritical Fluids, v. 40, p. 232-238, 2007. Disponível em: https://www.sciencedirect.com/science/article/abs/pii/S0896844606001641?via%3Dihub. Acesso em: 08 abr. 2021. https://doi.org/10.1016/j.supflu.2006.07.001
dc.identifier.uri.fl_str_mv https://repositorio.ufrn.br/handle/123456789/32548
dc.identifier.issn.none.fl_str_mv 0896-8446
dc.identifier.doi.none.fl_str_mv 10.1016/j.supflu.2006.07.001
identifier_str_mv PEREIRA, C. G.; ROSA, P.T.V. ; MEIRELES, M.A.A. . Extraction and isolation of indole alkaloids from Tabernaemontana catharinensis A.DC.: Technical and economical analysis. The Journal of Supercritical Fluids, v. 40, p. 232-238, 2007. Disponível em: https://www.sciencedirect.com/science/article/abs/pii/S0896844606001641?via%3Dihub. Acesso em: 08 abr. 2021. https://doi.org/10.1016/j.supflu.2006.07.001
0896-8446
10.1016/j.supflu.2006.07.001
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