重选尾矿细泥锡石浮选回收实验

邢姜, 邓久帅, 张浩, 王体琛, 黄艳, 吴伯增. 重选尾矿细泥锡石浮选回收实验[J]. 矿产综合利用, 2025, 46(2): 65-71. doi: 10.3969/j.issn.1000-6532.2025.02.010
引用本文: 邢姜, 邓久帅, 张浩, 王体琛, 黄艳, 吴伯增. 重选尾矿细泥锡石浮选回收实验[J]. 矿产综合利用, 2025, 46(2): 65-71. doi: 10.3969/j.issn.1000-6532.2025.02.010
XING Jiang, DENG Jiushuai, ZHANG Hao, WANG Tichen, HUANG Yan, WU Bozeng. Flotation Recovery of Fine Slime Cassiterite from Gravity Tailings[J]. Multipurpose Utilization of Mineral Resources, 2025, 46(2): 65-71. doi: 10.3969/j.issn.1000-6532.2025.02.010
Citation: XING Jiang, DENG Jiushuai, ZHANG Hao, WANG Tichen, HUANG Yan, WU Bozeng. Flotation Recovery of Fine Slime Cassiterite from Gravity Tailings[J]. Multipurpose Utilization of Mineral Resources, 2025, 46(2): 65-71. doi: 10.3969/j.issn.1000-6532.2025.02.010

重选尾矿细泥锡石浮选回收实验

  • 基金项目: 国家自然科学基金面上项目(52274283)
详细信息
    作者简介: 邢姜(2000-),女,硕士研究生,研究方向为矿产资源综合利用
    通讯作者: 邓久帅(1983-),男,教授,博士生导师,主要从事矿产资源综合利用等研究工作
  • 中图分类号: TD952

Flotation Recovery of Fine Slime Cassiterite from Gravity Tailings

More Information
  • 广西大厂矿区选厂在生产中采用摇床重选的方法对锡石进行回收,存在锡石难选、细泥损失大等问题。为强化尾矿中细粒级锡石的回收,提高锡选别作业的回收率,对该选厂摇床重选得到的尾矿开展了锡石细泥回收浮选实验研究。实验结果表明,通过“预先脱硫-锡石浮选”工艺流程,在条件实验的基础上,确定采用2 000 g/t捕收剂,800 g/t活化剂和6 g/t具有消泡功能的辅助捕收剂药剂制度进行浮锡实验,最终重选尾矿选锡闭路实验得到锡品位为7.41%,回收率47.61%的锡精矿,指标良好,经济可行。

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  • 图 1  脱硫条件实验流程

    Figure 1. 

    图 2  不脱硫条件实验流程

    Figure 2. 

    图 3  活化剂用量对锡石浮选指标的影响

    Figure 3. 

    图 4  捕收剂用量对锡石浮选指标的影响

    Figure 4. 

    图 5  P86用量对锡石浮选指标的影响

    Figure 5. 

    图 6  浮选回收闭路实验流程

    Figure 6. 

    表 1  尾矿试样的化学多元素分析/%

    Table 1.  Chemical multi-element analysis of tailings specimens

    SnPbSbZnSFeCaOSiO2
    0.760.100.140.242.3510.0341.7214.41
    下载: 导出CSV

    表 2  试样的矿物组成分析结果

    Table 2.  Mineral analysis of the samples

    矿物 锡石 磁黄
    铁矿
    方解石 黄铁矿 脆硫
    锑铅矿
    铁闪
    锌矿
    毒砂 石英
    含量/% 1.7 7.96 20.96 8.61 1.35 3.89 1.06 17.58
    下载: 导出CSV

    表 3  尾矿试样的粒度分析结果

    Table 3.  Results of particle size analysis of tailing samples

    粒级/mm产率/%锡品位/%锡分布率/%
    +0.07419.640.061.55
    -0.074+0.05621.140.328.88
    -0.056+0.04313.060.589.94
    -0.043+0.03115.811.2726.35
    -0.031+0.02111.001.2818.47
    -0.021+0.0105.841.5511.88
    -0.010+0.0082.921.284.91
    -0.00810.491.3118.02
    合计100.000.76100.00
    下载: 导出CSV

    表 4  脱硫与不脱硫浮锡实验结果

    Table 4.  Results of removal of sulfur and non-removal of sulfur during cassiterite flotation

    条件实验名称 产品 产率/% Sn S
    品位/% 回收率/% 品位/% 回收率/%
    脱硫浮锡 硫精矿 9.34 0.90 10.98 9.62 44.78
    锡精矿 7.14 4.28 39.89 6.05 38.95
    锡中矿 10.03 1.26 16.51 3.89 35.20
    尾矿 73.49 0.34 32.62 0.39 25.85
    给矿 100.00 0.77 100.00 2.01 100.00
    不脱硫浮锡 锡精矿 9.86 1.78 22.98 7.90 38.47
    锡中矿 31.53 0.78 31.77 2.41 37.51
    尾矿 58.61 0.59 45.25 0.83 24.02
    给矿 100.00 0.76 100.00 2.03 100.00
    下载: 导出CSV

    表 5  细泥系统脱硫尾矿综合条件闭路实验结果

    Table 5.  Results of the complete closed-circuit test of desulfurized tailings from the fine mud system

    产品名称 产率/% Sn S
    品位/% 回收率/% 品位/% 回收率/%
    硫精矿 12.36 1.18 18.63 9.42 51.75
    锡精矿 5.03 7.41 47.61 7.96 17.78
    锡尾矿 82.61 0.32 33.76 0.83 30.47
    给矿 100.00 0.78 100.00 2.25 100.00
    下载: 导出CSV
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出版历程
收稿日期:  2024-05-14
刊出日期:  2025-04-25

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