淮南矿区高灰高泥化炼焦煤深度脱泥工艺应用实践

    Study on application practice of deep desliming process for high-ash and high-argillaceous coking coal in Huainan mining area

    • 摘要: 为了解决“贫、细、杂”炼焦煤在分选中因高灰细泥干扰导致的精煤灰分高、分选效率低、浮选药剂消耗大等问题,淮河能源集团选煤分公司潘一选煤厂提出了将传统“双段弧形筛+脱泥两段浮选”工艺改造为“三质体电磁筛预处理+脱泥池深度脱泥+两段浮选”协同工艺。文章系统介绍了三质体电磁筛、脱泥池的结构组成与工作原理,以及两段浮选的工艺原理;再通过现场对比试验,探究各工艺环节的处理效果,对比改造前后工艺差异、三质体电磁筛与传统双段弧形筛的脱泥截留效果,分析脱泥池对浮选入料的优化作用及两段浮选的分选效能,并结合小筛分试验、生产指标监测等手段,验证工艺可行性与优越性。结果表明:相较于双段弧形筛,三质体电磁筛脱除高灰细泥、截留粗颗粒的效果更优,筛上煤泥灰分降至12.08%,> 0.5 mm粒级筛上产品产率达34.58%,粗精煤产率从27.33%提升至31.04%;脱泥池可高效脱除 < 0.045 mm粒级高灰细泥,溢流中该粒级产率达94.03%,底流灰分较入料降低1.79个百分点;两段浮选可实现精煤煤泥的高效分选,最终精煤灰分为10.52%,精煤产率、可燃体回收率、浮选完善指标分别为54.71%,73.70%,56.56%,二段浮选对各粒级精煤的降灰效果显著,尤其能有效脱除细粒级高灰细泥。“三质体电磁筛+脱泥两段浮选”协同工艺能适配淮南矿区高泥质炼焦煤分选需求,各工艺环节协同作用,可实现“降灰、提质、提产、降耗”的综合目标,解决了传统工艺分选精度低、药剂消耗大的痛点,工艺优化后年节约药剂费用20万元,净收益达18万元,为同类矿区选煤工艺优化升级提供了可复制的技术范式。

       

      Abstract: To solve the problems of high ash in clean coal, low separation efficiency, and high flotation reagent consumption caused by the interference of high-ash fine slime during the separation of "lean, fine, and complex" coking coal in the Huainan mining area, the Panyi Coal Preparation Plant of the Coal Preparation Branch of Huaihe Energy Group proposed transforming the traditional “double-stage sieve bend + two-stage desliming flotation” process into a combined process of “tri-mass electromagnetic screen pretreatment + desliming tank deep desliming + two-stage flotation.” The structural composition and working principles of the tri-mass electromagnetic screen and desliming tank, as well as the process principle of two-stage flotation, are systematically introduced. Through on-site comparative experiments, the treatment effects of each process stage were explored; the process differences before and after the transformation, and the desliming and retention effects of the tri-mass electromagnetic screen versus the traditional double-stage sieve bend were compared; the optimization effect of the desliming tank on flotation feed and the separation efficiency of two-stage flotation were analyzed; combined with small-scale screening tests and production index monitoring, the feasibility and superiority of the process were verified. The results show that: compared with the double-stage sieve bend, the tri-mass electromagnetic screen has a better effect on removing high-ash fine slime and retaining coarse particles, with the oversize slime ash content reduced to 12.08%, the oversize yield of the >0.5 mm size fraction reaching 34.58%, and the coarse clean coal yield increasing from 27.33% to 31.04%; the desliming tank can efficiently remove <0.045 mm high-ash fine slime, with the yield of this size fraction in the overflow reaching 94.03%, and the underflow ash content being 1.79 percentage points lower than the feed; two-stage flotation can achieve efficient separation of clean coal, with the final clean coal ash reaching 10.52%, and the clean coal yield, combustible recovery, and flotation perfection index being 54.71%, 73.70%, and 56.56%, respectively; the second-stage flotation has a significant ash reduction effect on all size fractions of clean coal, especially in effectively removing fine-grained high-ash slime. The combined process of "tri-mass electromagnetic screen + two-stage desliming flotation" matches the separation requirements of high-argillaceous coking coal in the Huainan mining area. The synergistic effect of each process stage can achieve the comprehensive goals of "ash reduction, quality improvement, yield enhancement, and consumption reduction," solving the pain points of low separation precision and high reagent consumption in traditional processes. After process optimization, the annual saving in reagent costs is 200 000 yuan, with a net profit of 180 000 yuan, providing a replicable technical paradigm for the optimization and upgrading of coal preparation processes in similar mining areas.

       

    /

    返回文章
    返回