Please use this identifier to cite or link to this item: http://localhost:8080/xmlui/handle/123456789/2630
Full metadata record
DC FieldValueLanguage
dc.contributor.authorKumar, Rayi Naveen-
dc.contributor.authorVinod, Ananthula Venu-
dc.date.accessioned2025-01-09T07:55:35Z-
dc.date.available2025-01-09T07:55:35Z-
dc.date.issued2014-
dc.identifier.citation10.3311/PPch.7122en_US
dc.identifier.urihttp://localhost:8080/xmlui/handle/123456789/2630-
dc.descriptionNITWen_US
dc.description.abstractIn the present study volumetric oxygen mass transfer coefficient kL a has been determined for biodegradation of phenol in a bubble column bioreactor. Experimental studies have been carried out at different i) feed concentrations of phenol, ii) air flow rates and iii) feed flow rates. Dynamic method has been used to determine the oxygen mass transfer coefficient. The mass transfer coefficient for oxygen obtained is in the range of 0.00513 – 0.01793 s-1. kL a was found to increase with increase in air flow rates and decrease with increase in feed concentration of phenol. The values obtained in this work are compared with the values available in literature. A mathematical correlation is derived for kL a in terms of dimensionless numbers.en_US
dc.language.isoenen_US
dc.publisherPeriodica Polytechnica Chemical Engineeringen_US
dc.subjectBiodegradation ·en_US
dc.subjectBioreactoren_US
dc.titleOxygen mass transfer in bubble column bioreactoren_US
dc.typeArticleen_US
Appears in Collections:Chemical Engineering

Files in This Item:
File Description SizeFormat 
Oxygen Mass Transfer in Bubble Column Bioreactor.pdf2.42 MBAdobe PDFView/Open


Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.