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Modeling and experimental studies on absorption of CO2 by Benfield solution in rotating packed bed

机译:旋转填充床中Benfield溶液吸收CO2的建模和实验研究

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This work presents the modeling and experimental investigation on absorption of CO2 by Benfield solution in rotating packed bed(RPB).A model was established to illustrate the mechanism of gas-liquid mass transfer with reactions in RPB at higher gravity level.Experiments were carried out at various rotating speeds,liquid flow rates,gas flow rates and temperatures in RPB,with Benfield solution as the absorbent.The validity of this model was demonstrated by the fact that most of the predicted y_o(mole fraction of CO2 in outlet gas)agreed well with the experimental data with a deviation within 10%.The presented profile of K_Ga(gas-phase volumetric mass transfer coefficient)along the radial direction of the packing could reasonably explain the end effect in RPB.As a result,this model is reliable in describing the removal of CO2 by Benfield solution in RPB at higher gravity level.
机译:这项工作提供了Benfield溶液在旋转填充床(RPB)中吸收CO2的建模和实验研究,建立了一个模型来说明在较高重力水平下RPB中气液传质反应的机理。在Benfield溶液作为吸收剂的情况下,在不同的转速,液体流速,气体流速和RPB中的温度。该模型的有效性通过以下事实证明了:大多数预测的y_o(出口气体中CO2的摩尔分数)都同意实验数据的偏差在10%以内。沿填料径向的K_Ga(气相体积传质系数)曲线可以合理地解释RPB的最终效应。因此,该模型是可靠的描述在较高重力水平下RPB中的Benfield溶液去除CO2的过程。

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