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M. Yoshimoto, S. Suenaga, K. Furumoto, K. Fukunaga and K. Nakao, “Gas-Liquid Interfacial Area, Bubble Size and Liquid-Phase Mass Transfer Coefficient in a ThreePhase External Loop Airlift Bubble Column,” Chemical and Biochemical Engineering Quarterly, Vol. 21, No. 4, 2007, pp. 365-372.

has been cited by the following article:

• TITLE: CFD Simulation of Scale Influence on the Hydrodynamics of an Internal Loop Airlift Reactor

  AUTHORS: Reza Davarnejad, Ehsan Bagheripoor, Abolfazl Sahraei

  KEYWORDS: Internal Loop Airlift Reactor; Gas Hold-Up, CFD

  JOURNAL NAME: Engineering, Vol.4 No.10, October 10, 2012

  ABSTRACT: In this work, the overall gas hold-up in the riser and down-comer of three internal airlift reactors with a working volume of 10.5, 32 and 200 l at the range of temperatures 18℃ - 21℃, under atmospheric pressure was simulated using Com-putational Fluid Dynamics (CFD). The range of superficial gas velocity was 0.5 - 3 cm/s. The three reactors geometrically were similar to each other. CFD simulation and experimental data showed that the gas hold-up in the riser and down-comer increased by increasing the reactor scale. It was concluded that the simulated data were in good agreement with the experimental ones obtained from the literature.