Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column

Loop type bubble columns have good performance of liquid circulation and mass transfer by airlift effect, where the liquid circulation time is an important measurable characteristic parameter. This parameter is affected by the column construction, the aspect ratio of the column, the cross-sectional...

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Main Authors: Yamamoto Tatsumi, Kawasaki Hiroyuki, Mori Hidetoshi
Format: Article
Language:English
Published: EDP Sciences 2017-01-01
Series:E3S Web of Conferences
Online Access:https://doi.org/10.1051/e3sconf/20172200194
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spelling doaj-331e56bc07ef4f8a9f85a2a581454d672021-08-11T14:28:57ZengEDP SciencesE3S Web of Conferences2267-12422017-01-01220019410.1051/e3sconf/20172200194e3sconf_asee2017_00194Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble columnYamamoto TatsumiKawasaki HiroyukiMori HidetoshiLoop type bubble columns have good performance of liquid circulation and mass transfer by airlift effect, where the liquid circulation time is an important measurable characteristic parameter. This parameter is affected by the column construction, the aspect ratio of the column, the cross-sectional area ratio of down comer to riser (R), and the superficial gas velocity in the riser (UGR). In this work, the mean gas holdup and the liquid circulation time (TC) have been measured in four types of loop airlift type bubble column: concentric tube internal loop airlift type, rectangular internal loop airlift type, external loop airlift type, external loop airlift with separator. Air and tap water were used as gas and liquid phase, respectively. The results have demonstrated that the mean gas holdup in riser increases in proportion to UGR, and that it in downcomer changes according to the geometric parameters of each bubble column. TC has been found to conform to an empirical equation which depends on UGR and the length of draft tube or division plate in the region of 0.33 < R < 1.https://doi.org/10.1051/e3sconf/20172200194
collection DOAJ
language English
format Article
sources DOAJ
author Yamamoto Tatsumi
Kawasaki Hiroyuki
Mori Hidetoshi
spellingShingle Yamamoto Tatsumi
Kawasaki Hiroyuki
Mori Hidetoshi
Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
E3S Web of Conferences
author_facet Yamamoto Tatsumi
Kawasaki Hiroyuki
Mori Hidetoshi
author_sort Yamamoto Tatsumi
title Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
title_short Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
title_full Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
title_fullStr Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
title_full_unstemmed Influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
title_sort influence of cross-sectional ratio of down comer to riser on the efficiency of liquid circulation in loop air lift bubble column
publisher EDP Sciences
series E3S Web of Conferences
issn 2267-1242
publishDate 2017-01-01
description Loop type bubble columns have good performance of liquid circulation and mass transfer by airlift effect, where the liquid circulation time is an important measurable characteristic parameter. This parameter is affected by the column construction, the aspect ratio of the column, the cross-sectional area ratio of down comer to riser (R), and the superficial gas velocity in the riser (UGR). In this work, the mean gas holdup and the liquid circulation time (TC) have been measured in four types of loop airlift type bubble column: concentric tube internal loop airlift type, rectangular internal loop airlift type, external loop airlift type, external loop airlift with separator. Air and tap water were used as gas and liquid phase, respectively. The results have demonstrated that the mean gas holdup in riser increases in proportion to UGR, and that it in downcomer changes according to the geometric parameters of each bubble column. TC has been found to conform to an empirical equation which depends on UGR and the length of draft tube or division plate in the region of 0.33 < R < 1.
url https://doi.org/10.1051/e3sconf/20172200194
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AT kawasakihiroyuki influenceofcrosssectionalratioofdowncomertoriserontheefficiencyofliquidcirculationinloopairliftbubblecolumn
AT morihidetoshi influenceofcrosssectionalratioofdowncomertoriserontheefficiencyofliquidcirculationinloopairliftbubblecolumn
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