Gas-Liquid Interfacial Area, Bubble Size and Liquid-Phase Mass Transfer Coefficient in a Three-Phase External Loop Airlift Bubble Column

Chemical and biochemical engineering quarterly

K. Furumoto¹  K. Nakao¹  K. Fukunaga¹  M. Yoshimoto¹  S. Suenaga¹ 

关键词: External loop airlift;    three phase flow;    suspended solid particles;    interfacial area;    bubble size;    oxygen transfer coefficient;   

DOI  :  

来源: Croatian Society of Chemical Engineers

【 摘 要 】

Abstract The interfacial area a was measured by the sulfite oxidation method in a three-phase external loop airlift bubble column suspending completely the different concentrations of ion exchange resin particles in aqueous carboxymethyl cellulose (CMC) solutions with a wide range of viscosity. The column had been previously studied for the circulating liquid velocity UL, gas holdup εG and volumetric gas-liquid oxygen transfer coefficient kLa in the two- and three-phase systems. The average bubble size dB and oxygen transfer coefficient kL were obtained as dB = 6 εG/a and kL = (the previous kLa)/a, respectively. The similar studies were carried out in the internal loop airlift and normal bubble columns for comparison. The a values in the external loop airlift were found to be little affected by the column height and particles concentrations, and to decrease with increasing viscosity. All the three columns showed a linear dependence of a on εG. A simple correlation of a, dB or kL was proposed as a function of εG and viscosity for the external loop airlift as well as both internal loop airlift and normal columns. A well-known relationship between kL and dB was confirmed to hold independent of column types and operating conditions for a given two or three phase system.

【 授权许可】

Unknown