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Froth flotation of sphalerite: Collector concentration, gas dispersion and particle size effects

机译:闪锌矿的泡沫浮选:集尘器浓度,气体扩散和粒径影响

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摘要

This experimental work on sphalerite flotation investigated the effect on flotation performance of three particle size fractions, namely, coarse (d_(80) = 100 μm), medium (d_(80) = 39 μm) and fine (d_(80) = 15 μm), bubble size distribution, superficial air velocity, and collector dosage. Bubble size distributions were characterized with the image analysis technique. The two-phase (liquid-gas) centrifugal pump and frother addition (MIBC, 5-30 ppm) allowed generating bubble diameters between 150 and 1050 μm, and air holdup ranging from 0.2% and 1.3%. Main results showed that each particle-size distribution required an optimal bubble-size profile, and that sphalerite recovery proceeded from mechanisms involving true flotation (when J_g = 0.04 cm/s and 1.9 × 10~(-4) M SIPX). However, cluster-flotation occurs at high collector dosage (when J_g= 0.04 cm/s and d_(32) between 285 and 1030 μm), and requiring further investigation.
机译:闪锌矿浮选的这项实验工作研究了三种粒径级分对粗粒(d_(80)= 100μm),中等(d_(80)= 39μm)和精细(d_(80)= 15)的浮选性能的影响。 (μm),气泡大小分布,表面空气速度和收集器剂量。用图像分析技术表征气泡尺寸分布。两相(液-气)离心泵和起泡剂添加(MIBC,5-30 ppm)使气泡直径在150至1050μm之间,空气滞留率在0.2%至1.3%范围内。主要结果表明,每个粒度分布都需要一个最佳的气泡大小分布图,并且闪锌矿的回收是从涉及真正浮选的机理(当J_g = 0.04 cm / s和1.9×10〜(-4)M SIPX时)进行的。但是,簇集浮选发生在高捕集剂量下(当J_g = 0.04 cm / s和d_(32)在285和1030μm之间时),需要进一步研究。

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