杨家渠选煤厂粗煤泥分选系统的优化改造

    Optimization and renovation of the coarse coal slime separation system at Yangjiaqu Coal Preparation Pant

    • 摘要: 为了解决粗煤泥分选效率低导致精煤灰分易超标、产量不足的问题,保障精煤质量(灰分 ≤ 8.5%)并提升选煤厂经济效益,杨家渠选煤厂采用“问题诊断-分环节改造”路径优化系统:对水力分级入料开展粒度、红外光谱及XRD分析,更换破损脱泥筛筛板并改造旋流器入料桶风力搅拌系统,解决 > 1 mm粗粒混入问题,为水力分级旋流器搭建“浓度-压力”闭环智能控制系统(控制浓度为250 ± 10 g/L、压力为0.15 ± 0.02 MPa),从而改善底流夹细现象;为螺旋分选机增设底流箱自动补水装置,调整截料器至距中心轴300 mm位置,降低分选错配率。生产实践表明:改造后水力分级入料中 > 1 mm粒级产率从13.99%降至3.06%,旋流器底流 < 0.25 mm粒级产率减少了12.16个百分点;螺旋分选机精煤产率从45.84%提升至70.54%,提高了24.7个百分点,且精煤灰分稳定达标;经济效益突出,与产品以中煤为主的工况相比年增效益9 146万元,与现有掺配方式相比年增效益5 470万元。该次改造有效解决了粗煤泥分选系统核心问题,实现了精煤质量与产量的双重保障,其技术路径可为同类低阶动力煤选煤厂粗煤泥分选系统优化提供可靠参考。

       

      Abstract: To address issues of low separation efficiency in the coarse coal slime system—which led to easily exceeding the target ash content of clean coal and insufficient production, and to ensure clean coal quality (ash content ≤ 8.5%) while enhancing the economic performance of the plant, Yangjiaqu Coal Preparation Plant optimized the system through a "problem diagnosis–stepwise renovation" approach. Specific measures included: conducting particle size distribution, infrared spectroscopy, and XRD analysis of the hydroclassification feed; replacing damaged screen plates on the desliming screen and modifying the pneumatic agitation system of the cyclone feed tank to reduce contamination by greater than 1 mm coarse particles; implementing a closed-loop intelligent control system for the hydrocyclone based on "density–pressure" (target density 250 ± 10 g/L, pressure 0.15 ± 0.02 MPa) to minimize fine coal loss in the underflow; and equipping the spiral concentrator with an automatic water replenishment device for the underflow box while adjusting the cutter position to 300 mm from the central axis to reduce misplacement rates. Production practice shows that: the yield of > 1 mm particles in the hydroclassification feed decreased from 13.99% to 3.06%; the proportion of < 0.25 mm particles in the cyclone underflow dropped by 12.16 percentage points; the clean coal yield of the spiral concentrator increased from 45.84% to 70.54%, a gain of 24.7 percentage points, with ash content consistently meeting standards. Economically, the renovation added annual benefits of 91.46 million yuan compared to a middlings-dominated product scenario and 54.70 million yuan compared to the existing blending method. The renovation effectively resolved core issues in the coarse coal slime separation system, ensuring both quality and yield of clean coal. The technical approach offers a reliable reference for optimizing similar coarse coal slime systems in low-rank thermal coal preparation plants.

       

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