Mass transfer characteristics of low <i>H/D</i> bubble columns

Abstract

Abstract The mass transfer characteristics of 0.2, 0.6 and 1.0 m diameter bubble columns having a low height to diameter ratio (0.6 &lt; H/D &lt; 4) and operated at low superficial gas velocities (0.01 &lt; V G &lt; 0.08 m/s) were investigated. Different types of spargers were used to study their effect on the column performance. The values of effective interfacial area, a , and volumetric mass transfer coefficient, k L a , were measured by using chemical methods. The values of a and k L a were found to vary from 40 to 420 m 2 /m 3 of clear liquid volume and from 0.01 to 0.16 s −1 , respectively, in the range of V G , and V L covered in this investigation. The value of the liquid‐side mass transfer coefficient, k L , was found to vary from 3 × 10 −4 to 7 × 10 4 m/s. The effect of the physical properties of the system on the values of a was also investigated. The height to diameter ratio and the column diameter did not have significant effect on the values of gas holdup, a and k L a . It was found that the sparger design is not of critical importance, provided multipoint/multiorifice gas spargers are used. The comparative performance of bubble columns having low H/D with horizontal sparged contactors and tall bubble columns has been considered.