dc.contributorLima, Alice Medeiros de
dc.contributorhttp://lattes.cnpq.br/0038936541518854
dc.contributorhttp://lattes.cnpq.br/6993669324122992
dc.creatorFujimoto, Marisa Cristina Mendonça
dc.date.accessioned2021-10-18T19:39:40Z
dc.date.accessioned2022-10-10T21:37:28Z
dc.date.available2021-10-18T19:39:40Z
dc.date.available2022-10-10T21:37:28Z
dc.date.created2021-10-18T19:39:40Z
dc.date.issued2018-12-03
dc.identifierFUJIMOTO, Marisa Cristina Mendonça. Modelagem e simulação de biorreator para produção de ácido fumárico. 2018. Trabalho de Conclusão de Curso (Graduação em Engenharia Química) – Universidade Federal de São Carlos, São Carlos, 2018. Disponível em: https://repositorio.ufscar.br/handle/ufscar/15023.
dc.identifierhttps://repositorio.ufscar.br/handle/ufscar/15023
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/4045164
dc.description.abstractConsidering the current scenario where there is a growing pressure for industry to include sustentability in its inegotiable values, several companies have been investing in research and development of new, environmentally friendly, processes. In the focus of innovation there are routes with smaller energy and solvent consumption, and reduced generation of waste. In this context, the present study aims at evaluating the production of fumaric acid via fermentation; the compound is an intermediate currently obtained from petrochemical raw materials. The study was based on extensive bibliographic research about the types of micro-organisms capable of producing the chemical, and an appropriate kinetic model to describe growth and accummulation of product was chosen. As an adequate kinetic model was not readily available in literature, a simple model was adjusted in the software SimulaFerm using experimental information reported in articles. Then, the bioreactor model was implemented in Scilab environment, making use of constitutive equations (kinetic models), and mass balances pertinent to transient operation. This software was chosen due to its interface with the process simulator COCO (CAPE-OPEN to CAPEOPEN), which does not comprise in its basic unit operations batch reactions commonly present in fermentations. With the results obtained, it was possible to better understand the limitations and opportunities regarding the production of fumaric acid through this alternative route.
dc.languagepor
dc.publisherUniversidade Federal de São Carlos
dc.publisherUFSCar
dc.publisherCâmpus São Carlos
dc.publisherEngenharia Química - EQ
dc.rightshttp://creativecommons.org/licenses/by-nc-nd/3.0/br/
dc.rightsAttribution-NonCommercial-NoDerivs 3.0 Brazil
dc.subjectModelagem e simulação
dc.subjectÁcido fumárico
dc.subjectModeling and simulation
dc.subjectFumaric acid
dc.titleModelagem e simulação de biorreator para produção de ácido fumárico
dc.typeOtros


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