Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures

Due to the ocurrence of a non ideal behavior of ethanol, butanol and acetone in aqueous solutions, a method to predict those properties in mixture that depend on the composition, temperature and pressure, especially the activity and the fugacity, is outlined in this work. These properties are very i...

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Fecha de publicación:
2018
Institución:
Universidad Pedagógica y Tecnológica de Colombia
Repositorio:
RiUPTC: Repositorio Institucional UPTC
Idioma:
spa
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oai:repositorio.uptc.edu.co:001/15249
Acceso en línea:
https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/8063
https://repositorio.uptc.edu.co/handle/001/15249
Palabra clave:
Butanol
actividad
fugacidad
azeótropo
sistema cuaternario.
Butanol
Activity
fugacity, azeotrope, quaternary system
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http://purl.org/coar/access_right/c_abf2
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oai_identifier_str oai:repositorio.uptc.edu.co:001/15249
network_acronym_str REPOUPTC2
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repository_id_str
dc.title.en-US.fl_str_mv Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
dc.title.es-ES.fl_str_mv Equilibrio líquido-vapor para el sistema cuaternario Agua-Acetona-Butanol-Etanol a Presiones Reducidas.
title Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
spellingShingle Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
Butanol
actividad
fugacidad
azeótropo
sistema cuaternario.
Butanol
Activity
fugacity, azeotrope, quaternary system
title_short Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
title_full Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
title_fullStr Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
title_full_unstemmed Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
title_sort Liquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low Pressures
dc.subject.es-ES.fl_str_mv Butanol
actividad
fugacidad
azeótropo
sistema cuaternario.
topic Butanol
actividad
fugacidad
azeótropo
sistema cuaternario.
Butanol
Activity
fugacity, azeotrope, quaternary system
dc.subject.en-US.fl_str_mv Butanol
Activity
fugacity, azeotrope, quaternary system
description Due to the ocurrence of a non ideal behavior of ethanol, butanol and acetone in aqueous solutions, a method to predict those properties in mixture that depend on the composition, temperature and pressure, especially the activity and the fugacity, is outlined in this work. These properties are very important for estimating equilibrium constants, constants of transfer speed and chemical reaction, sizing and design of process equipment. Currently, biobutanol is considered a substitute for bioethanol as a biofuel, presenting advantages, such as: higher heat capacity and lower vapor pressure. It is obtained from the fermentation of Acetone-Butanol-Ethanol (ABE), where its major products are acetone, butanol and ethanol in a molar ratio of 3: 6: 1, respectively. Therefore, the liquid-vapor equilibrium for the quaternary system water-acetone- butanol-ethanol was calculated at reduced pressures of 0.1, 0.5 and 1 kPa, with the purpose of evaluating the behavior of the azeotropes (water-butanol and water-ethanol), which is a key issue in the application of a separation process. The Non Random Two Liquid model (NRTL) was used to calculate the activity coefficient of the components in the liquid phase, the virial equations to calculate the fugacity coefficient of the components in the vapor phase and the Rachford and Rice algorithm for the dew temperature. In this way, it could be demonstrated that at low pressures the azeotrope formed between water and butanol slighly disappears while the pressure is going down. Therfore, it is recommended by using a pressure of 0.1 kPa for vacuum distillation, while 0.5 kPa for pervaportation. These values depend on the separation system stability (membranes in case of pervaporation) and the process economical balance.
publishDate 2018
dc.date.accessioned.none.fl_str_mv 2024-07-08T14:23:55Z
dc.date.available.none.fl_str_mv 2024-07-08T14:23:55Z
dc.date.none.fl_str_mv 2018-12-27
dc.type.none.fl_str_mv info:eu-repo/semantics/article
dc.type.coarversion.fl_str_mv http://purl.org/coar/version/c_970fb48d4fbd8a85
dc.type.coar.fl_str_mv http://purl.org/coar/resource_type/c_2df8fbb1
dc.identifier.none.fl_str_mv https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/8063
10.19053/01217488.v10.n1.2019.8063
dc.identifier.uri.none.fl_str_mv https://repositorio.uptc.edu.co/handle/001/15249
url https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/8063
https://repositorio.uptc.edu.co/handle/001/15249
identifier_str_mv 10.19053/01217488.v10.n1.2019.8063
dc.language.none.fl_str_mv spa
dc.language.iso.none.fl_str_mv spa
language spa
dc.relation.none.fl_str_mv https://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/8063/8301
dc.rights.coar.fl_str_mv http://purl.org/coar/access_right/c_abf2
rights_invalid_str_mv http://purl.org/coar/access_right/c_abf2
dc.format.none.fl_str_mv application/pdf
dc.publisher.es-ES.fl_str_mv Universidad Pedagógica y Tecnológica de Colombia
dc.source.en-US.fl_str_mv Ciencia En Desarrollo; Vol. 10 No. 1 (2019): Vol 10, Núm. 1 (2019): Enero - Junio; 103-116
dc.source.es-ES.fl_str_mv Ciencia en Desarrollo; Vol. 10 Núm. 1 (2019): Vol 10, Núm. 1 (2019): Enero - Junio; 103-116
dc.source.none.fl_str_mv 2462-7658
0121-7488
institution Universidad Pedagógica y Tecnológica de Colombia
repository.name.fl_str_mv Repositorio Institucional UPTC
repository.mail.fl_str_mv repositorio.uptc@uptc.edu.co
_version_ 1839633888012402688
spelling 2018-12-272024-07-08T14:23:55Z2024-07-08T14:23:55Zhttps://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/806310.19053/01217488.v10.n1.2019.8063https://repositorio.uptc.edu.co/handle/001/15249Due to the ocurrence of a non ideal behavior of ethanol, butanol and acetone in aqueous solutions, a method to predict those properties in mixture that depend on the composition, temperature and pressure, especially the activity and the fugacity, is outlined in this work. These properties are very important for estimating equilibrium constants, constants of transfer speed and chemical reaction, sizing and design of process equipment. Currently, biobutanol is considered a substitute for bioethanol as a biofuel, presenting advantages, such as: higher heat capacity and lower vapor pressure. It is obtained from the fermentation of Acetone-Butanol-Ethanol (ABE), where its major products are acetone, butanol and ethanol in a molar ratio of 3: 6: 1, respectively. Therefore, the liquid-vapor equilibrium for the quaternary system water-acetone- butanol-ethanol was calculated at reduced pressures of 0.1, 0.5 and 1 kPa, with the purpose of evaluating the behavior of the azeotropes (water-butanol and water-ethanol), which is a key issue in the application of a separation process. The Non Random Two Liquid model (NRTL) was used to calculate the activity coefficient of the components in the liquid phase, the virial equations to calculate the fugacity coefficient of the components in the vapor phase and the Rachford and Rice algorithm for the dew temperature. In this way, it could be demonstrated that at low pressures the azeotrope formed between water and butanol slighly disappears while the pressure is going down. Therfore, it is recommended by using a pressure of 0.1 kPa for vacuum distillation, while 0.5 kPa for pervaportation. These values depend on the separation system stability (membranes in case of pervaporation) and the process economical balance.Debido a la existencia de un comportamiento o interacción no ideal del etanol, butanol y acetona en soluciones acuosas, se presenta en este trabajo un método para predecir aquellas propiedades en mezcla que dependen de la composición, temperatura y presión, especialmente la actividad y la fugacidad. Estas propiedades son importantes para estimar constantes de equilibrio, constantes de velocidad de transferencia y reacción química, dimensionamiento y diseño de equipos de proceso. Actualmente, el biobutanol se considera un sustituto del bioetanol como biocombustible al presentar ventajas como mayor capacidadcalorífica y menor presión de vapor. Su obtención se realiza a partir de la fermentación Acetona-Butanol-Etanol (ABE), donde sus productos mayoritarios son acetona, butanol y etanol en una relación molar 3:6:1, respectivamente. Por ello, se calculó el equilibrio líquido-vapor para el sistema cuaternario agua-acetona- butanol-etanol a presiones reducidas de 0.1, 0.5 y 1 kPa, con el propósito de evaluar el comportamiento de los azeótropos (agua-butanol y agua-etanol), los cuales como bien se conocen límitan la aplicación de unproceso de separación. Se utilizó el modelo Non Random Two Liquid (NRTL) para calcular el coeficiente de actividad de los componentes en fase líquida, las ecuaciones del virial para calcular el coeficiente defugacidad de los componentes en fase de vapor y el algoritmo Rachford y Rice para el punto de roció. De esta manera, se pudo demostrar que a presiones bajas el azeótropo que se forma entre agua y butanol desaparece paulatinamente mientras se reduce la presión. Por tanto, se recomienda utilizar una presión de 0.1 kPa para la destilación al vacío y 0,5 kPa para la pervaporacion. Estos valores están condicionados a la estabilidad del medio de separación (membrana en el caso de la pervaporación) y a la evaluación económica del proceso.application/pdfspaspaUniversidad Pedagógica y Tecnológica de Colombiahttps://revistas.uptc.edu.co/index.php/ciencia_en_desarrollo/article/view/8063/8301Ciencia En Desarrollo; Vol. 10 No. 1 (2019): Vol 10, Núm. 1 (2019): Enero - Junio; 103-116Ciencia en Desarrollo; Vol. 10 Núm. 1 (2019): Vol 10, Núm. 1 (2019): Enero - Junio; 103-1162462-76580121-7488Butanolactividadfugacidadazeótroposistema cuaternario.ButanolActivityfugacity, azeotrope, quaternary systemLiquid-vapor equilibrium for the Water-Acetone-Butanol-Ethanol quaternary system at Low PressuresEquilibrio líquido-vapor para el sistema cuaternario Agua-Acetona-Butanol-Etanol a Presiones Reducidas.info:eu-repo/semantics/articlehttp://purl.org/coar/version/c_970fb48d4fbd8a85http://purl.org/coar/resource_type/c_2df8fbb1http://purl.org/coar/access_right/c_abf2Moreno Cascante, Jorge ArturoCubillos Lobo, Jairo Antonio001/15249oai:repositorio.uptc.edu.co:001/152492025-07-18 10:56:46.218metadata.onlyhttps://repositorio.uptc.edu.coRepositorio Institucional UPTCrepositorio.uptc@uptc.edu.co