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作 者:杨辉 王燕[1] 李震 朱怀工[1] 蔡旺锋[1] YANG Hui;WANG Yan;LI Zhen;ZHU Huai-gong;CAI Wang-feng(School of Chemical Engineering,Tianjin University,Tianjin 300350,China;Neimenggu Hulunbeier Dongneng Chemical Co.,Ltd.,Hulunbeier 021500,Neimenggu,China)
机构地区:[1]天津大学化工学院,天津300350 [2]内蒙古呼伦贝尔东能化工有限公司,内蒙古呼伦贝尔021500
出 处:《化学工程》2018年第10期16-20,共5页Chemical Engineering(China)
摘 要:针对一种新型旋流传质元件的溢流管高度和壳体上液相出口位置、面积及数量进行了流体力学性能优化实验研究。在直径500 mm的有机玻璃塔内,以空气-水为实验物系对具有不同壳体结构的传质元件进行了流体力学性能实验。在相同的液相负荷时,实验测定了不同气相负荷条件下传质元件的湿板压降、漏液率及雾沫夹带率。实验结果揭示了元件壳体上不同的液相出口位置和出口面积等参数以及不同的溢流管高度对湿板压降、漏液和雾沫夹带的影响规律。结果表明:当传质元件的溢流管底端距离盲板50 mm,壳体上液相出口位置距离叶片30 mm,液相出口数量为2、总面积为1. 88×10~4mm^2时的传质元件性能最优。An experimental optimization of hydrodynamic performance for a new type mass transfer cell was studied in terms of the height of the overflow pipe and the position,number and area of the liquid outlet on the shell.The hydrodynamic tests were carried out using an air-water system in a column constructed by polymethyl methacrylate with diameter of 500 mm.Under the same liquid loading condition,the wet plate pressure drop,the weeping rate and the entrainment rate were measured for mass transfer cell with different structural parameters at different gas loading conditions.The experimental results show the laws of the wet plate pressure drop,the weeping rate and the entrainment rate when the structure of the mass transfer cell is different.The performance of final cell structure is the best when the distance between the bottom of overflow pipe and blind plate is 50 mm,the distance between the liquid outlet and the blades is 30 mm,the number of liquid phase outlets is 2,and the liquid outlets area is 1.88×10 4 mm 2 on the shell.
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