王伟, 孙华峰, 李海军. 分选硫铁矿用高密度重介悬浮液特性的分析研究[J]. 选煤技术, 2018, 46(6): 42-45,50. DOI: 10.16447/j.cnki.cpt.2018.06.009
    引用本文: 王伟, 孙华峰, 李海军. 分选硫铁矿用高密度重介悬浮液特性的分析研究[J]. 选煤技术, 2018, 46(6): 42-45,50. DOI: 10.16447/j.cnki.cpt.2018.06.009
    WANG Wei, SUN Huafeng, LI Haijun. Analytical study on characteristics of high-density heavy medium suspension for separation of pyrite[J]. Coal Preparation Technology, 2018, 46(6): 42-45,50. DOI: 10.16447/j.cnki.cpt.2018.06.009
    Citation: WANG Wei, SUN Huafeng, LI Haijun. Analytical study on characteristics of high-density heavy medium suspension for separation of pyrite[J]. Coal Preparation Technology, 2018, 46(6): 42-45,50. DOI: 10.16447/j.cnki.cpt.2018.06.009

    分选硫铁矿用高密度重介悬浮液特性的分析研究

    Analytical study on characteristics of high-density heavy medium suspension for separation of pyrite

    • 摘要: 为了探究分选高硫煤矸石硫铁矿用高密度重介悬浮液的流变性与稳定性,寻找最佳工艺参数,对密度为1.8~2.3 g/cm3、非磁性物含量在10%~35%范围内的高密度重介悬浮液进行了系统研究。结果表明:高密度重介悬浮液的流变性和稳定性与选煤用低密度重介悬浮液相似,即悬浮液的密度和非磁性物含量越高,悬浮液的黏度越大,稳定性越好;分选高硫煤矸石硫铁矿时,采用磁铁矿粉和高硫煤矸石原生矿泥配制的高密度重介悬浮液,其密度宜控制在2.2 g/cm3以内,非磁性物含量宜控制在25%以内。

       

      Abstract: In order to investigate the rheological property and stability of high-density heavy medium suspension for separation of high-sulfur coal refuse, and determine the most appropriate technological process parameters, a systematic study is made of the high-density medium suspension having a density of 1.8-2.3 g/cm3 and a content of nonmagnetic materials in a range of 10%-35%. Study result indicates that: the rheological property and stability of the medium suspension varies in a pattern similar to that of the low-density suspension for separation of coal, namely, the higher the density of suspension, and the higher the content of nonmagnetic materials, the higher the viscosity and stability of the suspension become; and for the separation of pyrite from high-sulfur coal refuse, the density and content of nonmagnetic materials of the medium suspension prepared with magnetite powder and high-sulfur primary refuse fines should preferably be controlled within the range of 2.2 g/cm3 and 25% respectively.

       

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