马超, 王文宾, 董连平, 李志红. 常村煤矿选煤厂煤泥浮选药剂制度优化研究[J]. 选煤技术, 2018, 46(2): 27-29,33. DOI: 10.16447/j.cnki.cpt.2018.02.006
    引用本文: 马超, 王文宾, 董连平, 李志红. 常村煤矿选煤厂煤泥浮选药剂制度优化研究[J]. 选煤技术, 2018, 46(2): 27-29,33. DOI: 10.16447/j.cnki.cpt.2018.02.006
    MA Chao, WANG Wenbin, DONG Lianping, LI Zhihong. Optimization of the coal slime flotation reagent regime at Changcun Mine Coal Preparation Plant[J]. Coal Preparation Technology, 2018, 46(2): 27-29,33. DOI: 10.16447/j.cnki.cpt.2018.02.006
    Citation: MA Chao, WANG Wenbin, DONG Lianping, LI Zhihong. Optimization of the coal slime flotation reagent regime at Changcun Mine Coal Preparation Plant[J]. Coal Preparation Technology, 2018, 46(2): 27-29,33. DOI: 10.16447/j.cnki.cpt.2018.02.006

    常村煤矿选煤厂煤泥浮选药剂制度优化研究

    Optimization of the coal slime flotation reagent regime at Changcun Mine Coal Preparation Plant

    • 摘要: 常村煤矿选煤厂< 0.25 mm原生煤泥中< 0.045 mm细泥含量偏高,矿物组成以石英和高岭石为主,通过实验室浮选试验对药剂种类和用量进行了优化研究。结果表明:不同药剂对煤泥浮选的作用效果不同,且药剂之间存在一定的交互作用。采用现场药剂组合,捕收剂和起泡剂用量分别为600、80 g/t时,浮选精煤产率为70.42%、灰分为7.70%,尾煤灰分仅为46.51%;而在相同药剂用量条件下,现场捕收剂与仲辛醇起泡剂组合可获得产率为85.38%、灰分为9.43%的精煤,尾煤灰分高达75.52%,分选指标优于煤油与仲辛醇组合;而将现场起泡剂与煤油捕收剂进行组合时,浮选精煤产率为69.86%、灰分为7.72%,尾煤灰分46.68%。

       

      Abstract: The < 0.25 mm primary slime for treating in flotation circuit of the plant contains a relatively high proportion of < 0.045 mm fine size particles which is composed predominantly of quartz and kaolin. For selection of optimum kinds of reagent and determination of optimum dosages, laboratory flotation experiment is conducted. Test result shows that the flotation performance varies, depending on the use of reagents, and there exists a certain interaction between reagents. When industrial collector and frother are used in combination with a respective dosage of 600、80 g/t, the yield and ash of flotation concentrate are 70.42% and 7.70% respectively while the ash of tailings is only lowered to 46.51%. Yet, when collector is used together with frother secondary caprylic alcohol, with a respective dosage being the same as in the former case, the yield and ash of concentrate goes up to 85.38% and 9.43% respectively while the ash of tailings is as high as 75.52%, achieving a flotation performance much better than in the case of using kerosene secondary caprylic alcohol. Whereas, with the combined use of frother and kerosene, the yield and ash of concentrate is 69.86% and 7.72% respectively while the ash of tailings is 46.68%.

       

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