Relation between volumetric mass transfer coefficient and power input per unit volume for converging-diverging tube airlift fermenter

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DC Field	Value	Language
dc.contributor.author	Ghosh, Tapan K.	-
dc.contributor.author	Bhattacharyya, Bimal C.	-
dc.date.accessioned	2019-06-10T04:58:05Z	-
dc.date.available	2019-06-10T04:58:05Z	-
dc.date.issued	2010	-
dc.identifier.issn	1542-6580	-
dc.identifier.uri	http://172.16.0.4:8085/heritage/handle/123456789/3244	-
dc.description.abstract	A conventional external loop uniform tube airlift fermenter (UT-ALF) was modified to improve its performance. The riser part was replaced by a convergingdiverging tube. The newly developed reactor system is named a convergingdiverging tube airlift fermenter (CDT–ALF). The modified bioreactor (CDT–ALF) provides a unique hydrodynamic characteristic. Empirical correlation was developed to determine KLa with respect to power input per unit volume. The modified system (CDT-ALF) shows 250% higher KLa compared to conventional one.	en_US
dc.language.iso	en	en_US
dc.relation.ispartofseries	Vol. 10;Note S6	-
dc.subject	Airlift Fermenter	en_US
dc.subject	Bioreactor	en_US
dc.subject	Mass Transfer Coefficient	en_US
dc.title	Relation between volumetric mass transfer coefficient and power input per unit volume for converging-diverging tube airlift fermenter	en_US
dc.title.alternative	(In) INTERNATIONAL JOURNAL OF CHEMICAL REACTOR ENGINEERING	en_US
dc.type	Article	en_US
Appears in Collections:	Biotechnology (Publications)

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