浮选尾煤预先脱泥及研磨再浮试验研究

    Experimental study on pre-desliming by regrinding-reflotation of flotation tailings

    • 摘要: 为解决选煤厂浮选尾煤堆存固废资源化利用水平不足、炼焦煤有价资源流失严重、常规尾煤再浮选因高灰细泥罩盖干扰造成分选指标较差的行业难题,突破现有尾煤再选工艺仅粗粒磨矿、未预处理细粒高灰黏土矿物的技术短板,实现浮选尾煤中炼焦精煤资源高效回收利用。以开滦集团吕家坨煤矿浮选尾煤为试验原料,采用小直径水力旋流器预先脱泥+搅拌磨细磨解离的联合分选工艺,依次开展原料粒度组成与矿物组分检测试验、水力旋流器脱泥条件试验、搅拌磨矿试验、浮选可浮性对比试验。研究结果表明:ϕ75 mm水力旋流器在入料压力为0.25 MPa、入料矿浆质量分数为15%的最佳工况下,底流产率为36.16%、溢流产率为63.84%,溢流与底流产品灰分差可达17.25个百分点,高灰细泥组分集中富集于溢流,实现高效脱除;旋流器底流物料经搅拌磨研磨4 min后,物料体积平均粒径降至75.16 μm,相比原浮选尾煤粒径减小了47.42 μm,煤与石英、高岭石等脉石矿物解离程度显著提升;在限定精煤灰分为12.50%的条件下,底流脱泥研磨后浮选精煤产率可达40%,相较于原尾煤直接浮选的精煤产率提升35个百分点。采用水力旋流器前置脱泥可预先脱除高岭石类高灰细泥杂质,消除细泥罩盖对浮选体系的负面影响,后续磨矿作业能够有效解离嵌布连生体,二者组合工艺可大幅改善浮选入料矿物组成与粒度特性,提升浮选尾煤中炼焦精煤的回收效率,为存量浮选尾煤资源化回收开辟新型工艺路径。

       

      Abstract: To address the industry challenges of low solid waste utilization and significant loss of combustible coal resources caused by stockpiled flotation tailings in coal preparation plants, as well as the poor separation efficiency of conventional re-flotation due to high-ash fine slime interference, this study aims to break through the technical limitations of existing tailings re-separation processes, which only involve coarse-grain grinding without the pretreatment of fine-grained high-ash clay minerals. The ultimate goal is to achieve the highly efficient recovery and utilization of coking clean coal resources from flotation tailings. A combined separation process consisting of pre-desliming with a small-diameter hydrocyclone and fine grinding-liberation with a stirred mill was adopted. Using the flotation tailings from the Lvjiatuo Coal Mine of Kailuan Group as the experimental raw material, a series of experiments were sequentially conducted, including raw material particle size and mineral composition analysis, hydrocyclone desliming condition tests, stirred milling tests, and comparative flotation washability tests. The research results indicate that under the optimal operating conditions of a ϕ75 mm hydrocyclone—with a feed pressure of 0.25 MPa and a feed slurry mass concentration of 15%—the underflow and overflow yields are 36.16% and 63.84%, respectively. The ash content difference between the underflow and overflow products reaches up to 17.25 percentage point, demonstrating that the high-ash fine slime components are heavily enriched and effectively removed in the overflow. After grinding the hydrocyclone underflow material in the stirred mill for 4 min, the volume mean particle size of the material decreases to 75.16 μm, which is a reduction of 47.42 μm compared to the original flotation tailings, significantly enhancing the degree of liberation between coal and gangue minerals such as quartz and kaolinite. Under the target product specification limiting the clean coal ash content to 12.50%, the flotation clean coal yield of the deslimed and ground underflow can reach 40%, representing a 35 percentage point increase compared to the clean coal yield obtained from the direct flotation of the original tailings. Front-end desliming using a hydrocyclone can pre-remove kaolinite-type high-ash fine slime impurities, thereby eliminating the negative coating effects of fine slime on the flotation system. Meanwhile, the subsequent milling operation effectively liberates interlocked middlings (composite particles). The combination of these two processes can dramatically improve the mineral composition and particle size characteristics of the flotation feed, substantially enhancing the recovery efficiency of coking clean coal from flotation tailings. This study opens up a novel process path for the resource-oriented recovery of stockpiled flotation tailings.

       

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