Mass transfer in gas-liquid flow in small-diameter tubes

dc.creator	Tortopidis, P.	en
dc.creator	Bontozoglou, V.	en
dc.date.accessioned	2015-11-23T10:50:06Z
dc.date.available	2015-11-23T10:50:06Z
dc.date.issued	1997
dc.identifier	10.1016/s0009-2509(97)00027-4
dc.identifier.issn	0009-2509
dc.identifier.uri	http://hdl.handle.net/11615/33678
dc.description.abstract	Data on the rate of liquid-phase controlled mass transfer in a small-diameter tube (ID 4 mm) are presented. The motivation is to model the performance of compact contact devices consisting of short, narrow passages. The mean volumetric mass transfer coefficient, K(L)a, is measured for a wide range of superficial gas and liquid velocities (U-GS = 0.1-30 m s(-1) and U-LS = 0.01-1 m s(-1)). Results are related to flow regime transitions and are correlated in terms of Jepsen's (1970, A.I.Ch.E. J. 16, 705-711) fractional energy dissipation parameter. (C) 1997 Elsevier Science Ltd. All rights reserved.	en
dc.source	Chemical Engineering Science	en
dc.source.uri	<Go to ISI>://WOS:A1997XK32800003
dc.subject	mass transfer	en
dc.subject	gas-liquid flow	en
dc.subject	small-diameter tubes	en
dc.subject	compact	en
dc.subject	contactors	en
dc.subject	pressure drop	en
dc.subject	flow regime transition	en
dc.subject	PIPES	en
dc.subject	Engineering, Chemical	en
dc.title	Mass transfer in gas-liquid flow in small-diameter tubes	en
dc.type	journalArticle	en

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