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RAPID BENEFICIATION OF COAL TAILINGS USING TWO-STAGE REFLUX FLOTATION

机译:使用两级回流浮选的煤尾的快速优选

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Attention towards beneficiatingfine coal currently sentto tailings has grown recently, motivated bythe need for improved plant yield, and improved environmental management (Mercuri et al., 2014). Historically, the major obstacles preventing feasible beneficiation of hydrocyclone overflow include firstly, the need to process low pulp density feed at a high volumetric rate, and secondly, the high level of ash rejection necessary in order to produce a saleable coal product. Previously the first obstacle has led to prohibitive capital cost and hence long pay-back times, while the second has led to significant risk in delivering product with a satisfactory calorific value via the mineral matter and moisture, and a robust separation performance. To overcome these challenges, advancements in fine particle beneficiation technology are required. One emerging technology, the Reflux Flotation Cell (RFC), offers a unique two-stage solution to rapidly separate and clean fine coal particles from low pulp density tailings. The first stage facilitates as a rougher to quickly concentrate the fine coal, and reduce the flotation footprint by a factor of five or more by enhancing the throughput rate per unit vessel area. The second stage facilitates the cleaning of the recovered coal to deliver a low ash coal product from the first stage product through an effective distribution of fluidization wash water. The RFC utilizes a system of inclined channels to enhance the bubble-liquid segregation rate through a novel application of the Boycott effect (Boycott, 1920), thus enabling significantly higher gas and liquid fluxes, and bubble surface area fluxes per unit vessel area compared to conventional flotation devices (Jiang et al., 2014). Bubbles entering the inclined channels located below the vertical compartment encounter an effective increase in vessel area, thus allowing entrained bubbles to rise to the top of the channels and return, or reflux, back to the vertical compartment and avoid their loss to the tailings. This phenomenon has shown to deliver high flotation throughput capacity, achieving feed fluxes of up to a ten times greater than used in conventional flotation (Dickinson et al., 2015). Furthermore, exceptional cleaningand slimes rejection has beendemonstrated throughthe application of uniformfluidization wash water delivered downwards through the RFC plenum chamber that formally encloses the top of the system (Galvin et al., 2014).
机译:目前Senttopingfine煤的注意力最近已经增加了尾矿,所以需要改善植物产量,改进环境管理(Mercuri等,2014)。从历史上看,预防水力旋流溢出的可行性效果的主要障碍首先,需要以高容量速率加工低纸浆密度进料,其次,为了产生可渗透煤产物所需的高水平排斥液。此前,第一个障碍导致了禁止的资本成本,因此长期回报时间,而第二次已经导致通过矿物质和水分提供令人满意的热值的产品,以及稳健的分离性能。为了克服这些挑战,需要精细粒子优势技术的进步。一种新兴技术,回流浮选电池(RFC),提供独特的两级解决方案,可从低纸浆密度尾矿快速分离和清洁细煤颗粒。第一阶段有助于作为快速浓缩细煤的粗糙,通过提高每单位血管区域的吞吐量率来减少五倍以上的浮选足迹。第二阶段有助于清洁回收的煤,通过有效分布流化洗涤水来从第一阶段产品中递送低灰煤产品。 RFC利用倾斜通道系统通过抵制效应(抵制,1920)的新应用来增强气泡 - 液体隔离速率,从而实现了明显更高的气体和液体助熔剂,与每单位容器面积的气泡表面区域通量相比传统的浮选装置(江等,2014)。进入位于垂直舱下方的倾斜通道的气泡遇到血管面积的有效增加,从而允许夹带的气泡升到通道的顶部并返回或回流回到垂直舱,并避免它们对尾矿的损失。这种现象表明,可以提供高浮动量的能力,比传统浮选在常规浮选中使用的饲料助量大于10倍(Dickinson等,2015)。此外,卓越的清洁剂抑制通过均匀氟化洗涤水通过正式包围系统顶部的RFC增压室(Galvin等,2014)的均匀氟化洗涤水而倾向于倾向于逐渐氟化的洗涤水。

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