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Application of New Inflection Point Method for Hydrodynamics Study in Slurry Bubble Column Reactors

机译:新拐点法在浆式鼓泡塔反应器流体力学研究中的应用

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摘要

Bubble column reactors are used in a wide variety of applications such as multiphase bioreactors, catalytic slurry reactors, and absorption processes. The superficial gas velocity-gas holdup relationship and transition point are two important parameters for characterizing the hydrodynamics of a bubble column reactor. In this study, systematic investigation of a nitrogen - water - glass beads bubble column was conducted using the Taguchi experimental design method. The L_(16) (45) orthogonal array was selected for experiments design. Results showed that the order of importance of parameters is as follows: bed porosity, the ratio of height to diameter, and superficial gas velocity. A novel mathematical model was developed using the experimental data and based on 4th order polynomial. This model was successfully used to obtain the transition point with a high accuracy. The results of the mathematical method were in close agreement with those of the drift flux method. For liquid level of H=12D and slurry content of 13 vol%, transition velocity of 2.98 cm/s was calculated using the presented method, while a velocity of 3.14 cm/s was obtained from the drift flux method.
机译:鼓泡塔反应器用于多种应用,例如多相生物反应器,催化淤浆反应器和吸收过程。表观气体速度-气体保持率关系和过渡点是表征鼓泡塔反应器的流体动力学的两个重要参数。在这项研究中,使用田口实验设计方法对氮气-水-玻璃珠气泡塔进行了系统研究。选择L_(16)(45)正交阵列进行实验设计。结果表明,参数的重要性顺序如下:床孔隙度,高径比和表观气速。利用实验数据并基于四阶多项式开发了一种新颖的数学模型。该模型已成功用于获得高精度的过渡点。数学方法的结果与漂移通量方法的结果非常一致。对于液位H = 12D和浆液含量为13 vol%的情况,使用所提出的方法计算的过渡速度为2.98 cm / s,而通过漂移通量法获得的速度为3.14 cm / s。

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