GAS ENTRAINMENT RATE AND FLOW PATTERN IN A PLUNGING LIQUID JET AERATION SYSTEM USING INCLINED NOZZLES

被引：25

作者：

KUSABIRAKI, D ^{[1
]}

MUROTA, M ^{[1
]}

OHNO, S ^{[1
]}

YAMAGIWA, K ^{[1
]}

YASUDA, M ^{[1
]}

OHKAWA, A ^{[1
]}

机构：

[1] NIIGATA UNIV,DEPT MAT & CHEM ENGN,NIIGATA 95021,JAPAN

来源：

JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | 1990年 / 23卷 / 06期

关键词：

CHEMICAL REACTOR; INCLINED LIQUID JET; GAS ENTRAINMENT RATE; JET SHAPE CHANGE; GAS SHEATH LENGTH; BUBBLE PENETRATION DEPTH; LIQUID VELOCITY DISTRIBUTION; FLOW PATTERN;

D O I：

10.1252/jcej.23.704

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

For an inclined plunging jet aeration system using liquids of low viscosity, the effects of operating conditions on the gas entrainment rate Q(g) when nozzles having various values of length-to-diameter ratio L(n)/D(n) were employed were evaluated experimentally. The changes in Q(g) were related to those in jet shape before plunging and the liquid velocity distribution at the point where the gas sheath breaks up. An empirical equation was presented to predict the penetration depth Z of bubbles entrained by the diffusing jet. Bubble entrainment behavior was further examined in terms of the liquid velocity distribution in the submerged two-phase region and the size of entrained bubbles.

引用

页码：704 / 710

页数：7

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