Bubble size distribution in laboratory scale flotation cells

被引:113
作者
Grau, RA [1 ]
Heiskanen, K [1 ]
机构
[1] Helsinki Univ Technol, TKK, Helsinki 02015, Finland
关键词
flotation bubbles; flotation frothers; flotation machines; SURFACE-AREA FLUX; SAUTER MEAN DIAMETER; AIR-FLOW RATE; FINE PARTICLES; GAS DISPERSION; IMPELLER SPEED; FROTHERS; VESSEL;
D O I
10.1016/j.mineng.2005.06.011
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Bubble size was measured in two lab scale cells using the HUT bubble size analyzer. The influence of operating conditions on bubble size was investigated. The Sauter mean bubble size was found to vary over the range of 1.2-2.9 mm. The experimental bubble size distributions were satisfactorily represented by the upper-limit distributions. The frothers were found to have a profound impact on bubble size. It seems that frothers not only prevent bubble coalescence, but they also, affect the bubble break-up process. The air flow rate was also found to have a strong influence on bubble size. The Sauter mean bubble diameter increased as the air flow rate increased. The Sauter mean bubble diameter was found to decrease with increasing impeller speed. The addition of quartz on the other hand was found to increase the size of bubbles, this effect was more evident at solid concentration exceeding 20% (kg/kg). The size of bubbles generated with the multi-mix and free-flow mechanisms were different at similar operating conditions, in a non-coalescing environment. The free-flow design generated broader bubble size distributions than the multi-mix mechanism. (c) 2005 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1164 / 1172
页数:9
相关论文
共 25 条
[1]   THE EFFECT OF BUBBLE-SIZE ON THE RATE OF FLOTATION OF FINE PARTICLES [J].
AHMED, N ;
JAMESON, GJ .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 1985, 14 (03) :195-215
[2]  
BRUIJN W, 1974, T I CHEM ENG-LOND, V52, P88
[3]   Effect of flotation frothers on bubble size and foam stability [J].
Cho, YS ;
Laskowski, JS .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 2002, 64 (2-3) :69-80
[4]   A model to relate the flotation rate constant and the bubble surface area flux in mechanical flotation cells [J].
Deglon, DA ;
Sawyerr, F ;
O'Connor, CT .
MINERALS ENGINEERING, 1999, 12 (06) :599-608
[5]   Review of hydrodynamics and gas dispersion in flotation cells on South African Platinum concentrators [J].
Deglon, DA ;
Egya-Mensah, D ;
Franzidis, JP .
MINERALS ENGINEERING, 2000, 13 (03) :235-244
[6]  
GOERING CE, 1978, T ASAE, V21, P209, DOI 10.13031/2013.35277
[7]   Studies on impeller type, impeller speed and air flow rate in an industrial scale flotation cell.: Part 5:: Validation of k-Sb relationship and effect of froth depth [J].
Gorain, BK ;
Napier-Munn, TJ ;
Franzidis, JP ;
Manlapig, EV .
MINERALS ENGINEERING, 1998, 11 (07) :615-626
[8]   Studies on impeller type, impeller speed and air flow rate in an industrial scale flotation cell .4. Effect of bubble surface area flux on flotation performance [J].
Gorain, BK ;
Franzidis, JP ;
Manlapig, EV .
MINERALS ENGINEERING, 1997, 10 (04) :367-379
[9]  
GRAINGERALLEN TJN, 1970, T I MIN METALL, V79, pC15
[10]   Gas dispersion measurements in a flotation cell [J].
Grau, RA ;
Heiskanen, K .
MINERALS ENGINEERING, 2003, 16 (11) :1081-1089