Fluidized bed desliming in fine particle flotation - Part III flotation of difficult to clean coal

被引:27
作者
Galvin, K. P. [1 ]
Harvey, N. G. [1 ]
Dickinson, J. E. [1 ]
机构
[1] Univ Newcastle, Newcastle Inst Energy & Resources, Ctr Adv Particle Proc & Transport, Callaghan, NSW 2308, Australia
基金
澳大利亚研究理事会;
关键词
Coal; Fine particle processing; Flotation machines; Froth flotation; BUBBLE-SIZE; SURFACE; FRIT;
D O I
10.1016/j.mineng.2014.02.008
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A novel flotation system was used to process fine coal feeds supplied from coal preparation plants. The system consisted of an inverted fluidized bed arranged above a system of inclined channels. High fluidization (wash water) fluxes were imposed through a distributor enclosing the free-surface, producing strong positive bias of up to 2.4 cm/s, ideal for desliming. High gas fluxes of up to 2.6 cm/s, in excess of the flooding condition, were also imposed. The presence of the inclined channels prevented the entrainment of gas bubbles into the tailings stream. This paper, which is the third in a series, examines, for the first time, the hydrodynamic performance of this system on two actual plant feeds, each known to be difficult to wash. The first feed was a poorly liberated coal with particle size <260 mu m and 69% feed ash. The second was a well liberated coal with nominal size <125 mu m and 83% less than 38 pm. The product ash was shown to decrease significantly with an increasing fluidization flux to gas flux ratio. The single stage flotation system demonstrated a performance capable of matching the Tree Flotation Curve with some cases in fact surpassing this result. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:94 / 101
页数:8
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