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 |