关键词: 气升式内环流反应器, 液体外循环, 流体力学特性

Abstract:

The profiles of gas holdup and bubble velocity depending on superficial gas velocity were investigated in an inner airlift reactor with a down tube and an annulus gas distributor.The experimental set-up was made of plexiglass with an inner diameter of 0.286 m and a height of 3.0 m.Air and tap water were used as gas and liquid phases, respectively.The results showed that the gas holdup increased with increasing superficial gas velocity within both inner and outer loops.The gas holdup in the inner loop, however, was much higher than that in the outer loop.The bubbles entering the inner loop from the outer loop could be neglected in the ranges of the operating conditions.When an annulus gas distributor and a down tube were installed in the conventional airlift reactor, the gas holdup increased and its distribution became uniform, which enhanced the interfacial area between gas and liquid phases and the turbulent intensity of multiphase flow.Therefore, the interphase transfer would be improved in the inner loop.Then, the profiles of gas holdup and bubble velocity were simulated by using the Euler-Euler model in the platform of ANSYS CFX10.0 software package and fair agreement between numerical and experimental data was obtained. These results implied that the CFD simulation based on the Euler-Euler model, accompanied with experimental measurement, could be used to develop and scale up this new kind of loop reactor.

Key words: 气升式内环流反应器, 液体外循环, 流体力学特性