Simulation of Carbon Dioxide Recovery and Purification Stage at Ethanol Production
| dc.creator | Cruz Llerena, Arletis | |
| dc.creator | Pérez Ones, Osney | |
| dc.creator | Zumalacárregui de Cárdenas, Lourdes | |
| dc.creator | Almira Barceló, Kendra | |
| dc.creator | Rosales Saborit, Diana Rosa | |
| dc.date | 2024-04-03 | |
| dc.date.accessioned | 2025-10-01T23:53:10Z | |
| dc.description | The recovery of carbon dioxide (CO2) in ethanol distilleries is an important factor that provides both economic and environmental benefits. This research aims to obtain a validated simulation model for evaluating the CO2 recovery and purification stage in a Cuban distillery. The methodology used includes obtaining and validating the simulation model in Aspen Hysys v.10.0, evaluating improvement alternatives, and performing a technical-economic analysis. The simulation utilized the NRTL method to estimate properties for the equilibrium between water and organic substances at low pressures in the liquid phase and ideal for the vapor phase, and the Antoine model was used for the refrigerant in low pressure systems, assuming ideal behavior in the liquid phase. The model was validated with real process data, with a maximum relative error of less than 8%. Five refrigeration cycle alternatives were evaluated using new refrigerants (R-404a, R-290, R-152a, R-600a, R-417a), and the influence of the operating variables on the performance indicators behavior of the refrigeration system was analyzed. The best alternative from a technical point of view was R-600a, but the results were inferior compared to the base case. The redesign of the refrigeration cycle using new refrigerants did not result in efficiencies greater than 60%. | en-US |
| dc.description | La recuperación de dióxido de carbono (CO2) en las destilerías de etanol es un factor importante que aporta beneficios económicos y ambientales. El objetivo de esta investigación fue obtener un modelo de simulación validado para la evaluación de la etapa de recuperación y purificación de CO2 en una destilería cubana. La metodología empleada consistió en obtención y validación del modelo de simulación en Aspen Hysys v.10.0, evaluación de alternativas de mejoras, y realización de un análisis técnico-económico. En el desarrollo de la simulación, se seleccionó NRTL para la estimación de las propiedades para el equilibrio entre el agua y las sustancias orgánicas a bajas presiones en la fase líquida e ideal para la fase vapor. Para el refrigerante, se seleccionó el modelo de Antoine, aplicable para sistemas a bajas presiones y considerando que el comportamiento de la fase líquida es ideal. El modelo de simulación obtenido en el caso base fue validado con los datos reales del proceso con un máximo error relativo inferior al 8 %. Se evaluaron cinco alternativas del ciclo de refrigeración en las que se emplearon nuevos refrigerantes (R-404a, R-290, R-152a, R-600a, R-417a) y se analizó la influencia de las variables de operación en los indicadores de comportamiento del sistema de refrigeración. Desde el punto de vista técnico, la mejor alternativa fue el R-600a, pero en comparación con el caso base, los resultados fueron inferiores. Con el empleo de los nuevos refrigerantes, al rediseñar el ciclo de refrigeración no se obtuvieron rendimientos superiores al 60%. | es-ES |
| dc.format | application/pdf | |
| dc.format | text/xml | |
| dc.format | application/zip | |
| dc.format | text/html | |
| dc.identifier | https://revistas.itm.edu.co/index.php/tecnologicas/article/view/2845 | |
| dc.identifier | 10.22430/22565337.2845 | |
| dc.identifier.uri | https://hdl.handle.net/20.500.12622/7886 | |
| dc.language | spa | |
| dc.publisher | Instituto Tecnológico Metropolitano (ITM) | es-ES |
| dc.relation | https://revistas.itm.edu.co/index.php/tecnologicas/article/view/2845/3140 | |
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| dc.relation | https://revistas.itm.edu.co/index.php/tecnologicas/article/view/2845/3281 | |
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| dc.rights | Derechos de autor 2024 TecnoLógicas | es-ES |
| dc.rights | https://creativecommons.org/licenses/by-nc-sa/4.0 | es-ES |
| dc.source | TecnoLógicas; Vol. 27 No. 59 (2024); e2845 | en-US |
| dc.source | TecnoLógicas; Vol. 27 Núm. 59 (2024); e2845 | es-ES |
| dc.source | 2256-5337 | |
| dc.source | 0123-7799 | |
| dc.subject | Producción de etanol | es-ES |
| dc.subject | recuperación de CO2 | es-ES |
| dc.subject | purificación de CO2 | es-ES |
| dc.subject | ciclo de refrigeración | es-ES |
| dc.subject | simulación de procesos | es-ES |
| dc.subject | Ethanol production | en-US |
| dc.subject | CO2 recovery | en-US |
| dc.subject | CO2 purification | en-US |
| dc.subject | refrigeration cycle | en-US |
| dc.subject | process simulation | en-US |
| dc.title | Simulation of Carbon Dioxide Recovery and Purification Stage at Ethanol Production | en-US |
| dc.title | Simulación de la etapa de recuperación y purificación de dióxido de carbono en la producción de etanol | es-ES |
| dc.type | info:eu-repo/semantics/article | |
| dc.type | info:eu-repo/semantics/publishedVersion | |
| dc.type | Research Papers | en-US |
| dc.type | Artículos de investigación | es-ES |
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