Supercritical Extraction Process of Allspice Essential Oil
Allspice essential oil was extracted with supercritical carbon dioxide (SC-CO2) in a static process at three different temperatures (308.15, 313.15, and 318.15 K) and four levels of pressure (100, 200, 300, and 360 bar). The amount of oil extracted was measured at intervals of 1, 2, 3, 4, 5, and 6 h...
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doaj-0da46da684d94dddbb24633eb06a314c2020-11-25T00:12:20ZengHindawi LimitedJournal of Chemistry2090-90632090-90712017-01-01201710.1155/2017/64716846471684Supercritical Extraction Process of Allspice Essential OilYasvet Y. Andrade-Avila0Julian Cruz-Olivares1César Pérez-Alonso2Ciro Humberto Ortiz-Estrada3María del Carmen Chaparro-Mercado4Facultad de Química, Universidad Autónoma del Estado de México, Paseo Colón Intersección Paseo Tollocan S/N, 50120 Toluca, MEX, MexicoFacultad de Química, Universidad Autónoma del Estado de México, Paseo Colón Intersección Paseo Tollocan S/N, 50120 Toluca, MEX, MexicoFacultad de Química, Universidad Autónoma del Estado de México, Paseo Colón Intersección Paseo Tollocan S/N, 50120 Toluca, MEX, MexicoSecretaría de Gobernación, CNS-Policía Federal, Sistema de Desarrollo Policial, Poniente 116-590, Edificio A, Tercer Piso, Col. Industrial Vallejo, Deleg. Azcapotzalco, 02300 Ciudad de México, MexicoDepartamento de Ingeniería y Ciencias Químicas, Universidad Iberoamericana, Prol. Paseo de la Reforma 880, Lomas de Santa Fe, Álvaro Obregón, 01219 Ciudad de México, MexicoAllspice essential oil was extracted with supercritical carbon dioxide (SC-CO2) in a static process at three different temperatures (308.15, 313.15, and 318.15 K) and four levels of pressure (100, 200, 300, and 360 bar). The amount of oil extracted was measured at intervals of 1, 2, 3, 4, 5, and 6 h; the most extraction yield reached was of 68.47% at 318.15 K, 360 bar, and 6 h of contact time. In this supercritical extraction process, the distribution coefficient (KD), the mean effective diffusion coefficient (Def), the energy of activation (Ea), the thermodynamic properties (ΔG0, ΔH0, and ΔS0), and the apparent solubility (S) expressed as mass fraction (w/w) were evaluated for the first time. At the equilibrium the experimental apparent solubility data were successfully correlated with the modified Chrastil equation.http://dx.doi.org/10.1155/2017/6471684 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Yasvet Y. Andrade-Avila Julian Cruz-Olivares César Pérez-Alonso Ciro Humberto Ortiz-Estrada María del Carmen Chaparro-Mercado |
spellingShingle |
Yasvet Y. Andrade-Avila Julian Cruz-Olivares César Pérez-Alonso Ciro Humberto Ortiz-Estrada María del Carmen Chaparro-Mercado Supercritical Extraction Process of Allspice Essential Oil Journal of Chemistry |
author_facet |
Yasvet Y. Andrade-Avila Julian Cruz-Olivares César Pérez-Alonso Ciro Humberto Ortiz-Estrada María del Carmen Chaparro-Mercado |
author_sort |
Yasvet Y. Andrade-Avila |
title |
Supercritical Extraction Process of Allspice Essential Oil |
title_short |
Supercritical Extraction Process of Allspice Essential Oil |
title_full |
Supercritical Extraction Process of Allspice Essential Oil |
title_fullStr |
Supercritical Extraction Process of Allspice Essential Oil |
title_full_unstemmed |
Supercritical Extraction Process of Allspice Essential Oil |
title_sort |
supercritical extraction process of allspice essential oil |
publisher |
Hindawi Limited |
series |
Journal of Chemistry |
issn |
2090-9063 2090-9071 |
publishDate |
2017-01-01 |
description |
Allspice essential oil was extracted with supercritical carbon dioxide (SC-CO2) in a static process at three different temperatures (308.15, 313.15, and 318.15 K) and four levels of pressure (100, 200, 300, and 360 bar). The amount of oil extracted was measured at intervals of 1, 2, 3, 4, 5, and 6 h; the most extraction yield reached was of 68.47% at 318.15 K, 360 bar, and 6 h of contact time. In this supercritical extraction process, the distribution coefficient (KD), the mean effective diffusion coefficient (Def), the energy of activation (Ea), the thermodynamic properties (ΔG0, ΔH0, and ΔS0), and the apparent solubility (S) expressed as mass fraction (w/w) were evaluated for the first time. At the equilibrium the experimental apparent solubility data were successfully correlated with the modified Chrastil equation. |
url |
http://dx.doi.org/10.1155/2017/6471684 |
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