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离子交换行为对溶质运移影响作用的实验研究

史绪山 康鸿源 潘欢迎 柴波

史绪山, 康鸿源, 潘欢迎, 柴波. 离子交换行为对溶质运移影响作用的实验研究[J]. 地质科技通报, 2023, 42(4): 162-169. doi: 10.19509/j.cnki.dzkq.tb20210697
引用本文: 史绪山, 康鸿源, 潘欢迎, 柴波. 离子交换行为对溶质运移影响作用的实验研究[J]. 地质科技通报, 2023, 42(4): 162-169. doi: 10.19509/j.cnki.dzkq.tb20210697
Shi Xushan, Kang Hongyuan, Pan Huanying, Chai Bo. Experimental study on the effect of ion exchange on solute transport in a sandy tank[J]. Bulletin of Geological Science and Technology, 2023, 42(4): 162-169. doi: 10.19509/j.cnki.dzkq.tb20210697
Citation: Shi Xushan, Kang Hongyuan, Pan Huanying, Chai Bo. Experimental study on the effect of ion exchange on solute transport in a sandy tank[J]. Bulletin of Geological Science and Technology, 2023, 42(4): 162-169. doi: 10.19509/j.cnki.dzkq.tb20210697

离子交换行为对溶质运移影响作用的实验研究

doi: 10.19509/j.cnki.dzkq.tb20210697
基金项目: 

国家自然科学基金项目 42172318

详细信息
    作者简介:

    史绪山(1992—), 男, 现正攻读水文地质学专业博士学位, 主要从事水岩相互作用下地质灾害成因机制研究工作。E-mail: xushan_shi@cug.edu.cn

    通讯作者:

    潘欢迎(1975—), 男, 副教授, 主要从事水文地质和环境地质领域的教学和科研工作。E-mail: phy75@163.com

  • 中图分类号: P641

Experimental study on the effect of ion exchange on solute transport in a sandy tank

  • 摘要:

    为研究河流阶地和洪积扇这类典型水力沉积单元污染物运移规律, 搭建了大尺寸室内渗流槽开展溶质运移实验。通过点投放NaNO3溶液模拟点源污染物在水力沉积物中的运移过程, 测定不同位置主要离子成分随时间的变化, 用于分析离子交换过程对于溶质运移的影响及溶质迁移规律。结果表明: 在运移过程中, NO32-属于保守性离子, 穿透曲线呈尖瘦形, Na+受阳离子交替吸附作用的显著影响, 峰形陡升缓降; 阳离子交替吸附作用降低了Na+的弥散度, 离子交替吸附作用对弥散度的影响随着运移距离的增加愈加明显; 运移初期高浓度Na+在砂层中能交换出相当数量的Ca2+, Mg2+, K+等离子; 运移后期阳离子交替吸附反应方向改变, 沉积砂层吸附水中的Ca2+, Mg2+, K+, 穿透曲线存在3种阳离子低于背景值的情况; 交替吸附作用使得对流-弥散作用下的Na+质量浓度穿透曲线形状更加宽缓, "拖尾"现象更为明显; 渗流砂槽内不同区域的水化学类型在空间上产生了差异性。研究成果对于开展水力沉积单元地下水污染防治具有一定指导意义。

     

  • 图 1  渗流槽系统物理模型

    a.实物图;b.模型示意图;c.定水头装置;d.溶质投放装置;e.取样装置

    Figure 1.  Physical model of the seepage tank

    图 2  监测孔布设位置示意图(1~9为监测孔)

    Figure 2.  Schematic diagram of the location of the monitoring holes

    图 3  阴离子质量浓度穿透曲线(分图中左上角编号②~⑨分别对应图 2中的2~9号监测孔)

    Figure 3.  Concentration breakthrough curve of anion

    图 4  阳离子质量浓度穿透曲线(分图中左上角编号同上)

    Figure 4.  Concentration breakthrough curve of cation

    图 5  交替吸附作用对Na+质量浓度的影响

    Figure 5.  Effect of cation exchange adsorption on the concentration of Na+

    表  1  渗流槽填充介质设计参数

    Table  1.   Design parameters of the filling medium of the seepage tank

    填充介质 几何参数 物理参数 矿物组成
    长/cm 宽/cm 高/cm 容重/(kg·m-3) 孔隙度/% 渗透系数/(m·s-1)
    黏土 150 100 40 1 830 58 10-7 高岭石、蒙脱石
    中砂 340 100 60~90 2 460 44 10-4 石英、长石
    砾石 100 100 20 2 650 28 2×10-4 石英、云母
    下载: 导出CSV

    表  2  监测孔布设位置坐标

    Table  2.   Coordinates of the monitoring holes locations

    监测孔编号 1 2 3 4 5 6 7 8 9
    x/cm 20 50 80 120 120 150 250 250 300
    y/cm 50 50 50 75 25 50 75 25 50
    z/cm 50 50 50 50 75 50 75 75 75
    注: 以模拟槽前端顶部近视点为坐标原点(见图 2),长度单位为cm
    下载: 导出CSV

    表  3  2, 3号监测孔Na+和NO32-的弥散度计算结果

    Table  3.   Calculation results of the dispersion of Na+ and NO32- in the No.2 and No.3 monitoring holes

    离子成分 x/m tm/h 实际流速v/(m·h-1) 弥散系数DL/(m2·h-1) 弥散度α/m
    Na+ 0.3 1.76 0.1 0.008 384 0.083 841
    0.6 3.56 0.016 381 0.163 809
    NO32- 0.3 1.75 0.1 0.008 482 0.084 821
    0.6 3.36 0.018 384 0.183 847
    下载: 导出CSV

    表  4  交替吸附作用对到达峰值时间的影响

    Table  4.   Effect of cation exchange adsorption on the peak time

    监测孔编号 2 3 4 6 7 8 9
    到达峰值时间tm/h NO32- 1.75 3.36 5.50 5.50 7.50 8.00 8.75
    Na+ 1.76 3.56 8.75 9.00 11.00
    延迟时间tdelay/h 0.01 0.20 1.25 1.00 2.25
    延迟时间比r/% 0.57 5.95 16.67 12.50 25.71
    注:延迟时间比$r=\frac{t_{\text {delay }}}{t_{\mathrm{m}}\left(\mathrm{NO}_3^{2-}\right)} \times 100 \% $
    下载: 导出CSV
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  • 收稿日期:  2021-11-08
  • 录用日期:  2023-01-30
  • 修回日期:  2022-04-29

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