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改性粉煤灰净化酸性矿山废水污染机理研究

王宪革 赵子千 沙浩群 何小松

王宪革,赵子千,沙浩群,等.改性粉煤灰净化酸性矿山废水污染机理研究[J].环境工程技术学报,2024,14(5):1635-1645 doi: 10.12153/j.issn.1674-991X.20240130
引用本文: 王宪革,赵子千,沙浩群,等.改性粉煤灰净化酸性矿山废水污染机理研究[J].环境工程技术学报,2024,14(5):1635-1645 doi: 10.12153/j.issn.1674-991X.20240130
WANG X G,ZHAO Z Q,SHA H Q,et al.Research on the mechanism of modified fly ash treatment of acid mine drainage pollution[J].Journal of Environmental Engineering Technology,2024,14(5):1635-1645 doi: 10.12153/j.issn.1674-991X.20240130
Citation: WANG X G,ZHAO Z Q,SHA H Q,et al.Research on the mechanism of modified fly ash treatment of acid mine drainage pollution[J].Journal of Environmental Engineering Technology,2024,14(5):1635-1645 doi: 10.12153/j.issn.1674-991X.20240130

改性粉煤灰净化酸性矿山废水污染机理研究

doi: 10.12153/j.issn.1674-991X.20240130
基金项目: 国家重点研发计划项目(2020YFC1806503)
详细信息
    作者简介:

    王宪革(1999—),男,硕士研究生,主要研究方向为固体废物处理处置及资源化,wxg0399@163.com

    通讯作者:

    何小松(1982—),男,研究员,博士,主要从事固体废物处理处置技术研究,hexs82@126.com

  • 中图分类号: X75

Research on the mechanism of modified fly ash treatment of acid mine drainage pollution

  • 摘要:

    煤矸石堆存过程中产生的酸性矿山废水(acid mine drainage,AMD)对周边水环境具有严重污染风险。基于“以废治废”理念,选择煤炭燃烧产生的粉煤灰开展了去除AMD中污染物的研究。针对粉煤灰原灰处理效果不佳的现状,对比了不同改性条件下的粉煤灰对AMD中污染物的去除效果,筛选出了去除效果最佳的粉煤灰改性材料,并从微观层面解析了粉煤灰改性材料去除污染物过程中的作用机理。结果显示:经Ca(OH)2助熔焙烧改性粉煤灰处理后,模拟AMD废水中的Fe、Mn含量由100 mg/L降至低于1 mg/L,污染物去除率达99%。Ca(OH)2助熔焙烧改性粉煤灰对Fe、Mn的吸附过程主要为单层化学吸附,在0~2 h内吸附接近平衡。此外,Ca(OH)2助熔焙烧改性增加了粉煤灰表面粗糙度和孔隙数量,并在表面形成六面体晶相结构。同时,Ca(OH)2助熔焙烧改性过程活化了粉煤灰颗粒表面Si和Al元素,提高了其Zeta电位,减少了游离羟基,增加了固定羟基,从而增强了其对污染物的吸附能力。Ca(OH)2助熔焙烧改性显著提高了粉煤灰对AMD中污染物的去除率,为粉煤灰治理AMD提供了材料与方法依据。

     

  • 图  1  不同材料和不同改性粉煤灰对AMD模拟废水的处理效果

    注:焙烧改性指焙烧改性粉煤灰,Na(OH)改性、Ca(OH)2改性分别指Na(OH)助熔焙烧改性、Ca(OH)2助熔焙烧改性粉煤灰。

    Figure  1.  Effectiveness of different materials and different modified fly ashes on AMD simulated wastewater treatment

    图  2  粉煤灰与Ca(OH)2焙烧改性粉煤灰对废水中Fe、Mn的等温吸附曲线

    Figure  2.  Isothermal adsorption curves of Fe and Mn in wastewater by fly ash and Ca(OH)2 flux-roasted modified fly ash

    图  3  粉煤灰和Ca(OH)2助熔焙烧改性粉煤灰对Fe、Mn的吸附效果及等温模型拟合曲线

    Figure  3.  Adsorption effects of fly ash and Ca(OH)2 flux-roasted modified fly ash on Fe and Mn and isothermal model fitting curves

    图  4  粉煤灰和Ca(OH)2焙烧改性粉煤灰对Mn和Fe的吸附动力学拟合曲线

    Figure  4.  Fitting curves of adsorption kinetics of fly ash and Ca (OH)2 flux-roasted modified fly ash on Mn and Fe

    图  5  粉煤灰和Ca(OH)2助熔焙烧改性粉煤灰对Fe、Mn的动力学吸附拟合曲线

    Figure  5.  Fitted curves of kinetic adsorption of fly ash and Ca(OH)2 flux-roasted modified fly ash on Fe and Mn

    图  6  粉煤灰、焙烧改性粉煤灰以及Ca(OH)2助熔焙烧改性粉煤灰3种材料的SEM图

    Figure  6.  SEM images of three materials: fly ash, roasted modified fly ash and Ca(OH)2 flux-roasted modified fly ash

    图  7  粉煤灰、焙烧粉煤灰以及Ca(OH)2助熔焙烧改性粉煤灰氮吸附脱附曲线

    Figure  7.  Nitrogen adsorption desorption of fly ash, roasted fly ash and Ca(OH)2 flux-roasted modified fly ash

    图  8  经不同处理后粉煤灰的孔径及Zeta电位分布

    Figure  8.  Pore size and Zeta potential distribution of fly ash after different treatments

    图  9  不同改性条件和不同应用条件下粉煤灰的傅里叶红外光谱图

    Figure  9.  Fourier infrared spectra of fly ash under different modification conditions and different application conditions

    图  10  粉煤灰、焙烧改性粉煤灰及Ca(OH)2助熔焙烧改性粉煤灰的XRD谱图

    Figure  10.  XRD spectra of fly ash, roasted modified fly ash and Ca(OH)2 flux-roasted modified fly ash

    表  1  粉煤灰、焙烧改性粉煤灰和Ca(OH)2助熔焙烧改性粉煤灰比表面积

    Table  1.   Specific surface areas of fly ash, roasted modified fly ash and Ca(OH)2 flux-roasted modified fly ash

    材料比表面积/(m2/g)
    粉煤灰0.713 2
    焙烧改性粉煤灰0.556 5
    Ca(OH)2改性粉煤灰10.881 3
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  • 收稿日期:  2024-03-01
  • 录用日期:  2024-05-15
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