Effect of Liquid Viscosity on Back Flow Rate and Exchange Rate of Liquid in a Vertical Stirred Vessel with Six Impellers

被引：4

作者：

Ohira, Yuichi ^{[1
]}

Shimadzu, Masamitsu ^{[1
]}

Obata, Eiji ^{[1
]}

Ando, Koji ^{[1
]}

机构：

[1] Muroran Inst Technol, Div Appl Sci, Grad Sch Engn, Muroran, Hokkaido 0508585, Japan

来源：

KAGAKU KOGAKU RONBUNSHU | 2013年 / 39卷 / 01期

关键词：

Stirred Vessel; Multiple Impeller; Back Flow Rate; Exchange Rate; Liquid Viscosity; MULTIPLE IMPELLERS; BUBBLE-COLUMN; MIXER;

D O I：

10.1252/kakoronbunshu.39.13

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

By applying a backmixing model to the liquid mixing characteristics of vertical vessels with six impellers, the effect of liquid viscosity on the back flow rate and the exchange rate of liquid was experimentally investigated. The vessel diameter D-T was 0.10 m and the impeller diameter D-i was one-half of the vessel diameter D-T. The relationship among the back flow rate f, the feed flow rate q and the exchange rate Q was established as f=Q-q/2 for carboxymethyl cellulose solution and starch syrup solution as an agitated liquid. The modified dimensionless exchange rate of vertical vessels with six impellers Q/(nD(i)(3)A(r)) was proportional to the agitated Reynolds number N-Re to the power of 0.0, 0.50 and 1.0, depending on the range of N-Re.

引用

页码：13 / 17

页数：5

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