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Gas holdup and volumetric oxygen transfer coefficient in a three-phase fluidized bed bioreactor
1988
Journal of Chemical Engineering of Japan
The gas-liquid volumetric oxygen transfer coefficient in a three-phase fluidized bed bioreactor was studied using Ca-alginate gels as the solid phase. The coefficient, kLa, in three-phase fluidized beds was smaller than that in bubble columns, regardless of gel diameter. This result was a new finding, and was shown to be characteristic of low-density gel beds. The value of kLa decreased with decreasing gel diameter and with increasing particle concentration in the liquid suspension. This
doi:10.1252/jcej.21.15
fatcat:ge3qef2i5rhdpjiag4yok7svga