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    超細全尾砂深錐動態絮凝濃密試驗

    王洪江 王小林 張璽 吳愛祥 田志剛 杜向紅

    王洪江, 王小林, 張璽, 吳愛祥, 田志剛, 杜向紅. 超細全尾砂深錐動態絮凝濃密試驗[J]. 工程科學學報, 2022, 44(2): 163-169. doi: 10.13374/j.issn2095-9389.2020.11.05.005
    引用本文: 王洪江, 王小林, 張璽, 吳愛祥, 田志剛, 杜向紅. 超細全尾砂深錐動態絮凝濃密試驗[J]. 工程科學學報, 2022, 44(2): 163-169. doi: 10.13374/j.issn2095-9389.2020.11.05.005
    WANG Hong-jiang, WANG Xiao-lin, ZHANG Xi, WU Ai-xiang, TIAN Zhi-gang, DU Xiang-hong. Deep cone dynamic flocculation thickening of ultrafine full tailings[J]. Chinese Journal of Engineering, 2022, 44(2): 163-169. doi: 10.13374/j.issn2095-9389.2020.11.05.005
    Citation: WANG Hong-jiang, WANG Xiao-lin, ZHANG Xi, WU Ai-xiang, TIAN Zhi-gang, DU Xiang-hong. Deep cone dynamic flocculation thickening of ultrafine full tailings[J]. Chinese Journal of Engineering, 2022, 44(2): 163-169. doi: 10.13374/j.issn2095-9389.2020.11.05.005

    超細全尾砂深錐動態絮凝濃密試驗

    doi: 10.13374/j.issn2095-9389.2020.11.05.005
    基金項目: 國家自然科學基金資助項目(51834001)
    詳細信息
      通訊作者:

      王小林,E-mail: 18706841567@163.com

      張璽,E-mail: 544484377@qq.com

    • 中圖分類號: TD853

    Deep cone dynamic flocculation thickening of ultrafine full tailings

    More Information
    • 摘要: 為探明超細全尾砂的濃密特性,開展量筒沉降實驗,小型和半工業深錐動態濃密試驗。結果表明,分子量1200萬的非離子型絮凝劑最利于尾砂沉降,隨絮凝劑單耗增加,溢流濁度降低,底流濃度基本不變。隨固體通量增加,溢流濁度增加,底流濃度降低。固體通量0.4 t·m?2·h?1,給料固體質量分數12%,絮凝劑單耗50 g·t?1的最佳參數條件下,小型和半工業動態濃密試驗的底流平均固體質量分數分別為62.8%和74.4%,泥層高度對底流濃度影響顯著。深錐濃密機底流固體質量分數隨泥層高度增加呈DoseResp函數增長,分為緩慢增長(泥層1~4 m)、快速增長(泥層4~7 m)和基本穩定(泥層超過7~8 m)3個階段,這跟尾砂絮團在不同泥層高度下的壓縮性能有關。可根據底流濃度與泥層高度的函數關系,調節泥層高度來滿足井下充填所需底流濃度。

       

    • 圖  1  全尾砂粒度分布曲線

      Figure  1.  Particle size distribution of full tailings

      圖  2  實驗裝置。(a)小型動態濃密裝置;(b)半工業深錐濃密裝置

      Figure  2.  Experimental facility: (a) small-scale dynamic thickener; (b) semi-industrial deep cone thickener

      圖  3  不同類型絮凝劑作用下的尾砂沉降高度曲線

      Figure  3.  Settlement height curve of tailings under the action of different types of flocculants

      圖  4  固體通量與給料固體質量分數關系

      Figure  4.  Relationship between the solid flux and feeding solid mass fraction

      圖  5  尾砂沉降速度與絮凝劑單耗關系

      Figure  5.  Relationship between the settling velocity of tailings and flocculant dosage

      圖  6  深錐濃密機底流固體質量分數與泥層高度關系

      Figure  6.  Relationship between the solid mass fraction of underflow and mud height in the deep cone thickener

      圖  7  尾砂絮團的簡單立體結構。(a)平面圖;(b)側面圖

      Figure  7.  Simple three-dimensional structure of tailings flocs: (a) plan; (b) side

      圖  8  尾砂絮團的錐體結構。(a)平面圖;(b)側面圖

      Figure  8.  Pyramidal structure of tailings flocs: (a) plan; (b) side

      表  1  小型動態濃密實驗方案和結果

      Table  1.   Small-scale dynamic thickening: experiment scheme and results

      Solid flux /
      (t·m?2·h?1)
      Flocculant dosage /
      (g·t?1)
      Average turbidity of
      overflow/10?6
      Average solid mass
      fraction of
      underflow /%
      0.24069.261.0
      0.36040.761.0
      0.430184.560.5
      0.55077.359.5
      下載: 導出CSV
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    • 收稿日期:  2020-11-05
    • 網絡出版日期:  2021-02-20
    • 刊出日期:  2022-02-15

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