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Diseño de un proceso de enriquecimiento de biogás mediante captura de dióxido de carbono

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dc.contributor.advisor Tinoco, Diana , Director
dc.contributor.author Alvarez Silva, Daniel Santiago
dc.contributor.author Townsend Cañola, Michael Enrique
dc.creator ESPOL
dc.date.accessioned 2023-10-26T16:13:22Z
dc.date.available 2023-10-26T16:13:22Z
dc.date.issued 2023
dc.identifier.citation Alvarez Silva, D. S. y Townsend Cañola, M. E. (2023). Diseño de un proceso de enriquecimiento de biogás mediante captura de dióxido de carbono. [Proyecto Integrador]. ESPOL.FCNM .
dc.identifier.uri http://www.dspace.espol.edu.ec/handle/123456789/58499
dc.description Este trabajo aborda la alta demanda energética en la industria avícola, especialmente en la empresa Avícola San Isidro S.A. (AVISID), cuyos sistemas de vapor emplean biogás generado in situ a partir de re
dc.format application/pdf
dc.format.extent 62 paginas
dc.language.iso spa
dc.publisher ESPOL
dc.rights openAccess
dc.subject PSA
dc.subject Aspen Adsorption
dc.subject Enriquecimiento biogás
dc.subject Sílica gel
dc.subject Captura de carbono
dc.title Diseño de un proceso de enriquecimiento de biogás mediante captura de dióxido de carbono
dc.type Ingeniero Químico
dc.identifier.codigoespol T-110539
dc.description.city Guayaquil
dc.description.degree Escuela Superior Politécnica del Litoral
dc.identifier.codigoproyectointegrador INGE-2014
dc.description.abstractenglish This work addresses the high energy demand in the poultry industry, particularly at Avícola San Isidro S.A. (AVISID), whose steam systems use on-site biogas generated from waste. However, the presence of CO2 in the biogas reduces its energy efficiency. The project aims to design a biogas enrichment method to generate steam more efficiently through the simulation of a Pressure Swing Adsorption (PSA) system using Aspen Plus and Aspen Adsorption V12.1® tools. This system will improve the biogas quality, reduce operational costs, and environmental impact. Separation methods such as amine scrubbing, PSA, and polymeric membranes were compared, and the simulation of the best method, a PSA system with silica gel as an adsorbent, was selected and replicated. A parametric study was conducted to demonstrate the effect of bed dimensions, cycle time, and product flow on methane purity and recovery percentages in the process. Subsequently, the system was sized for the study conditions, proposing a two-cycle PSA arrangement in series with results of biogas purity at 75.76% and methane recovery at 77.42%. Furthermore, steam generation relative to biogas cons


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