Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design
- Autores
- Díaz, María Soledad; Espinosa, Susana Noemi; Brignole, Esteban Alberto
- Año de publicación
- 2005
- Idioma
- inglés
- Tipo de recurso
- artículo
- Estado
- versión publicada
- Descripción
- In this work supercritical deterpenation of orange peel oil with carbon dioxide is studied. Optimal schemes and operating conditions are determined through the formulation of a nonlinear programming model that includes reliable thermodynamic predictions with a group contribution equation of state and rigorous unit models. A detailed comparison of binary and ternary equilibrium predictions with available experimental data is reported. Simulation results are in agreement with previous laboratory-scale separation values. Different solvent cycle schemes have been included in the mathematical model. Net profit is maximized taking into account capital and operating costs associated to the complete deterpenation process. Numerical results show that a compression cycle is the optimal solvent recovery system in all cases. Furthermore, optimal operating conditions have been determined in main units (extractor and separator), for the production of both a five-fold concentrate and a high purity aroma, as raffinate, respectively.
Fil: Díaz, María Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina
Fil: Espinosa, Susana Noemi. Universidad Nacional del Comahue; Argentina
Fil: Brignole, Esteban Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina - Materia
-
Co2
Deterpenation
Optimization
Orange Peel Oil
Supercritical Fluid Processes - Nivel de accesibilidad
- acceso abierto
- Condiciones de uso
- https://creativecommons.org/licenses/by-nc-sa/2.5/ar/
- Repositorio
- Institución
- Consejo Nacional de Investigaciones Científicas y Técnicas
- OAI Identificador
- oai:ri.conicet.gov.ar:11336/79071
Ver los metadatos del registro completo
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Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle designDíaz, María SoledadEspinosa, Susana NoemiBrignole, Esteban AlbertoCo2DeterpenationOptimizationOrange Peel OilSupercritical Fluid Processeshttps://purl.org/becyt/ford/2.4https://purl.org/becyt/ford/2In this work supercritical deterpenation of orange peel oil with carbon dioxide is studied. Optimal schemes and operating conditions are determined through the formulation of a nonlinear programming model that includes reliable thermodynamic predictions with a group contribution equation of state and rigorous unit models. A detailed comparison of binary and ternary equilibrium predictions with available experimental data is reported. Simulation results are in agreement with previous laboratory-scale separation values. Different solvent cycle schemes have been included in the mathematical model. Net profit is maximized taking into account capital and operating costs associated to the complete deterpenation process. Numerical results show that a compression cycle is the optimal solvent recovery system in all cases. Furthermore, optimal operating conditions have been determined in main units (extractor and separator), for the production of both a five-fold concentrate and a high purity aroma, as raffinate, respectively.Fil: Díaz, María Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaFil: Espinosa, Susana Noemi. Universidad Nacional del Comahue; ArgentinaFil: Brignole, Esteban Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; ArgentinaElsevier Science2005-08info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/resource_type/c_6501info:ar-repo/semantics/articuloapplication/pdfapplication/pdfapplication/pdfapplication/pdfhttp://hdl.handle.net/11336/79071Díaz, María Soledad; Espinosa, Susana Noemi; Brignole, Esteban Alberto; Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design; Elsevier Science; Journal of Supercritical Fluids; 35; 1; 8-2005; 49-610896-8446CONICET DigitalCONICETenginfo:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S0896844604003201info:eu-repo/semantics/altIdentifier/doi/10.1016/j.supflu.2004.12.002info:eu-repo/semantics/openAccesshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/reponame:CONICET Digital (CONICET)instname:Consejo Nacional de Investigaciones Científicas y Técnicas2025-09-03T10:00:04Zoai:ri.conicet.gov.ar:11336/79071instacron:CONICETInstitucionalhttp://ri.conicet.gov.ar/Organismo científico-tecnológicoNo correspondehttp://ri.conicet.gov.ar/oai/requestdasensio@conicet.gov.ar; lcarlino@conicet.gov.arArgentinaNo correspondeNo correspondeNo correspondeopendoar:34982025-09-03 10:00:04.527CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicasfalse |
dc.title.none.fl_str_mv |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
title |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
spellingShingle |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design Díaz, María Soledad Co2 Deterpenation Optimization Orange Peel Oil Supercritical Fluid Processes |
title_short |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
title_full |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
title_fullStr |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
title_full_unstemmed |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
title_sort |
Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design |
dc.creator.none.fl_str_mv |
Díaz, María Soledad Espinosa, Susana Noemi Brignole, Esteban Alberto |
author |
Díaz, María Soledad |
author_facet |
Díaz, María Soledad Espinosa, Susana Noemi Brignole, Esteban Alberto |
author_role |
author |
author2 |
Espinosa, Susana Noemi Brignole, Esteban Alberto |
author2_role |
author author |
dc.subject.none.fl_str_mv |
Co2 Deterpenation Optimization Orange Peel Oil Supercritical Fluid Processes |
topic |
Co2 Deterpenation Optimization Orange Peel Oil Supercritical Fluid Processes |
purl_subject.fl_str_mv |
https://purl.org/becyt/ford/2.4 https://purl.org/becyt/ford/2 |
dc.description.none.fl_txt_mv |
In this work supercritical deterpenation of orange peel oil with carbon dioxide is studied. Optimal schemes and operating conditions are determined through the formulation of a nonlinear programming model that includes reliable thermodynamic predictions with a group contribution equation of state and rigorous unit models. A detailed comparison of binary and ternary equilibrium predictions with available experimental data is reported. Simulation results are in agreement with previous laboratory-scale separation values. Different solvent cycle schemes have been included in the mathematical model. Net profit is maximized taking into account capital and operating costs associated to the complete deterpenation process. Numerical results show that a compression cycle is the optimal solvent recovery system in all cases. Furthermore, optimal operating conditions have been determined in main units (extractor and separator), for the production of both a five-fold concentrate and a high purity aroma, as raffinate, respectively. Fil: Díaz, María Soledad. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina Fil: Espinosa, Susana Noemi. Universidad Nacional del Comahue; Argentina Fil: Brignole, Esteban Alberto. Consejo Nacional de Investigaciones Científicas y Técnicas. Centro Científico Tecnológico Conicet - Bahía Blanca. Planta Piloto de Ingeniería Química. Universidad Nacional del Sur. Planta Piloto de Ingeniería Química; Argentina |
description |
In this work supercritical deterpenation of orange peel oil with carbon dioxide is studied. Optimal schemes and operating conditions are determined through the formulation of a nonlinear programming model that includes reliable thermodynamic predictions with a group contribution equation of state and rigorous unit models. A detailed comparison of binary and ternary equilibrium predictions with available experimental data is reported. Simulation results are in agreement with previous laboratory-scale separation values. Different solvent cycle schemes have been included in the mathematical model. Net profit is maximized taking into account capital and operating costs associated to the complete deterpenation process. Numerical results show that a compression cycle is the optimal solvent recovery system in all cases. Furthermore, optimal operating conditions have been determined in main units (extractor and separator), for the production of both a five-fold concentrate and a high purity aroma, as raffinate, respectively. |
publishDate |
2005 |
dc.date.none.fl_str_mv |
2005-08 |
dc.type.none.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/publishedVersion http://purl.org/coar/resource_type/c_6501 info:ar-repo/semantics/articulo |
format |
article |
status_str |
publishedVersion |
dc.identifier.none.fl_str_mv |
http://hdl.handle.net/11336/79071 Díaz, María Soledad; Espinosa, Susana Noemi; Brignole, Esteban Alberto; Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design; Elsevier Science; Journal of Supercritical Fluids; 35; 1; 8-2005; 49-61 0896-8446 CONICET Digital CONICET |
url |
http://hdl.handle.net/11336/79071 |
identifier_str_mv |
Díaz, María Soledad; Espinosa, Susana Noemi; Brignole, Esteban Alberto; Citrus peel oil deterpenation with supercritical fluids: Optimal process and solvent cycle design; Elsevier Science; Journal of Supercritical Fluids; 35; 1; 8-2005; 49-61 0896-8446 CONICET Digital CONICET |
dc.language.none.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
info:eu-repo/semantics/altIdentifier/url/https://www.sciencedirect.com/science/article/pii/S0896844604003201 info:eu-repo/semantics/altIdentifier/doi/10.1016/j.supflu.2004.12.002 |
dc.rights.none.fl_str_mv |
info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
eu_rights_str_mv |
openAccess |
rights_invalid_str_mv |
https://creativecommons.org/licenses/by-nc-sa/2.5/ar/ |
dc.format.none.fl_str_mv |
application/pdf application/pdf application/pdf application/pdf |
dc.publisher.none.fl_str_mv |
Elsevier Science |
publisher.none.fl_str_mv |
Elsevier Science |
dc.source.none.fl_str_mv |
reponame:CONICET Digital (CONICET) instname:Consejo Nacional de Investigaciones Científicas y Técnicas |
reponame_str |
CONICET Digital (CONICET) |
collection |
CONICET Digital (CONICET) |
instname_str |
Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.name.fl_str_mv |
CONICET Digital (CONICET) - Consejo Nacional de Investigaciones Científicas y Técnicas |
repository.mail.fl_str_mv |
dasensio@conicet.gov.ar; lcarlino@conicet.gov.ar |
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1842269617993547776 |
score |
13.13397 |