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化学工业与工程 1997, Vol. 14 Issue (2) :19-24    DOI:
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气-液-固三相搅拦槽中液相氧传递性能的研究
徐魁,戴干策,陈达美
华南理工大学化学工程系,华东理工大学联合化学反应工程研究所,广东工业大学化学工程系
Mass Transfer Characteristic of Oxygen in Liquid in Three-phase Stirred Vessels
Xu Kui
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摘要 在机械搅拌槽中使用翼形轴流桨(K4)、圆盘涡轮桨(DT)、6叶45°斜叶桨(6PTD、6PTU)(排出流向下,向上)对低粘度三相体系的液相氧传递性能与悬浮液浓度、通气水平及搅拌功率之间的变化规律作了实验研究。实验得出:K1a∝(Pg/V)k;当悬浮液浓度没有使液相表观粘性产生明显改变时,颗粒的存在、通气量的提高都有助于K1a的提高。翼形桨由于较好的轴向分散及混合性能,在相同的搅拌功率输入下,K1a保持较高的水平。
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徐魁
戴干策
陈达美
关键词翼形轴流桨   斜叶桨   固体悬浮   液相氧传递性能     
Abstract: This article presents the influences of suspenson concentration, gas volume in liquid and power consumption on gas liquid mass transfer characteristic for low viscosity system using a new type axial impeller (K 4), 45°pitched blade disk turbine (pumping down and up) and disk turbine (DT) respectively in three phase stirred vessels, It is concluded that: K 1a∝(P g/V) k ; and if the apparent viscosity of suspension changes little due to the suspension concentration, the presence of solid makes the volumetric mass transfer coefficient K 1a increase, and K 1a is enhanced with the increasing of gas volume, Because the new type axial impeller (K 4) produces higher axial dispersion and mixing, the K 1a value keeps higher in same power consumption.
Keywordsaxial impeller 45° pitched blade disk turbine suspension of solid mass transfer characteristic of oxygen in liquid     
Received 1997-04-15;
引用本文:   
徐魁,戴干策,陈达美.气-液-固三相搅拦槽中液相氧传递性能的研究[J].  化学工业与工程, 1997,14(2): 19-24
Xu Kui .Mass Transfer Characteristic of Oxygen in Liquid in Three-phase Stirred Vessels[J].  Chemcial Industry and Engineering, 1997,14(2): 19-24
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