dc.creatorde Jesus
dc.creatorSergio S.; Moreira Neto
dc.creatorJoao; Santana
dc.creatorAline; Maciel Filho
dc.creatorRubens
dc.date2015-OCT
dc.date2016-06-07T13:19:27Z
dc.date2016-06-07T13:19:27Z
dc.date.accessioned2018-03-29T01:39:39Z
dc.date.available2018-03-29T01:39:39Z
dc.identifier
dc.identifierInfluence Of Impeller Type On Hydrodynamics And Gas-liquid Mass-transfer In Stirred Airlift Bioreactor. Wiley-blackwell, v. 61, p. 3159-3171 OCT-2015.
dc.identifier0001-1541
dc.identifierWOS:000360764800002
dc.identifier10.1002/aic.14871
dc.identifierhttp://onlinelibrary.wiley.com/doi/10.1002/aic.14871/epdf
dc.identifierhttp://repositorio.unicamp.br/jspui/handle/REPOSIP/242690
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1306388
dc.descriptionFundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
dc.descriptionThe influence of impeller type in a mechanically stirred airlift bioreactor was analyzed in relation to the non-Newtonian viscous fluids. The agitation was carried out through a marine impeller (axial impeller) and a paddle impeller (radial impeller) located along with the gas sparger in the region comprised by the riser. The bioreactor was sparged with air under different velocities (0.036-0.060 m s(-1)). Carboxymethylcellulose 1.94% and xanthan 1.80% were used as a fluid model. The gas holdup and volumetric mass-transfer coefficient increased in up to five and three times, respectively, when compared to a conventional airlift bioreactor; however, better results were obtained when the straight paddle impeller type was used. The results suggest that the studied bioreactor can be used successfully in viscous fluid, and it can be more efficient than conventional airlift bioreactors. The results obtained suggest the use of radial impellers. (c) 2015 American Institute of Chemical Engineers AIChE J, 61: 3159-3171, 2015
dc.description61
dc.description10
dc.description
dc.description3159
dc.description3171
dc.descriptionFundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
dc.descriptionFundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)
dc.descriptionFAPESP [2008/57873-8, 2010/04903-7, 2010/03764-3]
dc.description
dc.description
dc.description
dc.languageen
dc.publisherWILEY-BLACKWELL
dc.publisher
dc.publisherHOBOKEN
dc.relationAICHE JOURNAL
dc.rightsfechado
dc.sourceWOS
dc.subjectNon-newtonian Fluids
dc.subjectXanthan Gum Solutions
dc.subjectTransfer Coefficient
dc.subjectHold-up
dc.subjectOxygen-transfer
dc.subjectBubble-column
dc.subjectPower-consumption
dc.subjectMixing Time
dc.subjectTheoretical Prediction
dc.subjectFermentation Media
dc.titleInfluence Of Impeller Type On Hydrodynamics And Gas-liquid Mass-transfer In Stirred Airlift Bioreactor
dc.typeArtículos de revistas


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