Air Dispersion and Bubble Characteristics in a Downflow Flotation Column

被引:17
|
作者
Zhu, Hongzheng [1 ,2 ]
Lopez Valdivieso, Alejandro [2 ]
Zhu, Jinbo [1 ]
Min, Fanfei [1 ]
Song, Shaoxian [3 ]
Corona Arroyo, Mario Alberto [4 ]
机构
[1] Anhui Univ Sci & Technol, Sch Mat Sci & Engn, Huainan 232001, Peoples R China
[2] Univ Autonoma San Luis Potosi, Inst Met, Surface Chem Lab, San Luis Potosi 78000, Mexico
[3] Wuhan Univ Technol, Sch Resources & Environm Engn, Wuhan, Hubei, Peoples R China
[4] Univ Guanajuato, Dept Minas Met & Geol, Div Ingn, Guanajuato, Mexico
基金
中国国家自然科学基金;
关键词
Sauter mean diameter; aeration rate; DDA concentration; downflow flotation column; bubble; CRITICAL COALESCENCE CONCENTRATION; MASS-TRANSFER COEFFICIENT; GAS HOLDUP; MULTIPHASE FLOW; IMPELLER SPEED; ORE FLOTATION; SIZE; FROTHERS; PERFORMANCE; REACTOR;
D O I
10.1080/08827508.2018.1556159
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Bubble Sauter mean diameter and aeration rate of a gas-liquid system in a laboratory downflow flotation column were explored. Both critical coalescence concentration and Sauter mean diameter decreased with increasing superficial liquid velocity, and also the Sauter mean diameter was found to obviously increase with the increase in the sampling height under low dodecylamine concentration. The aeration rate increased as the dodecylamine concentration increased at a constant valve opening degree and also linearly increased as superficial air velocity increased at a constant superficial liquid velocity of 11 cm/s. Compared to the superficial air velocity, the dodecylamine concentration was found to present a larger effect on the Sauter mean diameter but a smaller one on the aeration rate within the studied ranges of the dodecylamine concentration and superficial air velocity.
引用
收藏
页码:224 / 229
页数:6
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