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改性无烟煤材料的制备及其对磷的吸附回收性能

武越 赵婷 金彦任 薛燕 张凌旋 李达 乔晋如 黄杨

武越,赵婷,金彦任,等.改性无烟煤材料的制备及其对磷的吸附回收性能[J].环境工程技术学报,2022,12(5):1653-1659 doi: 10.12153/j.issn.1674-991X.20210349
引用本文: 武越,赵婷,金彦任,等.改性无烟煤材料的制备及其对磷的吸附回收性能[J].环境工程技术学报,2022,12(5):1653-1659 doi: 10.12153/j.issn.1674-991X.20210349
WU Y,ZHAO T,JIN Y R,et al.Preparation of modified anthracites and research on their adsorption and recovery performance on phosphorus[J].Journal of Environmental Engineering Technology,2022,12(5):1653-1659 doi: 10.12153/j.issn.1674-991X.20210349
Citation: WU Y,ZHAO T,JIN Y R,et al.Preparation of modified anthracites and research on their adsorption and recovery performance on phosphorus[J].Journal of Environmental Engineering Technology,2022,12(5):1653-1659 doi: 10.12153/j.issn.1674-991X.20210349

改性无烟煤材料的制备及其对磷的吸附回收性能

doi: 10.12153/j.issn.1674-991X.20210349
基金项目: 国家自然科学基金青年基金项目(51708050)
详细信息
    作者简介:

    武越(1992—),男,工程师,硕士,主要从事吸附材料的开发与改性研究,1508235620@qq.com

    通讯作者:

    黄杨(1990—),女,副教授,博士,主要从事吸附机理研究,huangyang@cuit.edu.cn

  • 中图分类号: X703

Preparation of modified anthracites and research on their adsorption and recovery performance on phosphorus

  • 摘要:

    为了实现污水中磷的回收与资源化利用,提出采用Fe-Al-Zr改性的无烟煤材料吸附-回收磷的方法。该吸附剂对磷的总吸附量为13.022 mg/g,吸附机理主要包括静电作用、配体交换和表面沉积等;微孔提供主要的吸附位点,决定了磷的吸附容量。该吸附剂可循环使用4个周期,直至磷的吸附率低于50%。在碱性条件下,通过投加一定量的CaCl2〔Ca∶P(摩尔比)=2∶1〕,磷能够以羟基磷灰石(HAP)的形式脱附和被回收。

     

  • 图  1  原始无烟煤和Fe-Al-Zr改性无烟煤的SEM图像以及Fe-Al-Zr改性无烟煤的EDS谱图

    Figure  1.  SEM image of original anthracite and Fe-Al-Zr modified anthracite, and EDS mapping of Fe-Al-Zr modified anthracite

    图  2  原始无烟煤以及Fe-Al-Zr改性无烟煤吸附磷前后的XRD

    Figure  2.  XRD curve of origin anthracites and Fe-Al-Zr modified anthracites before and after adsorption

    图  3  原始无烟煤和Fe-Al-Zr改性无烟煤的投加量对磷去除率的影响

    Figure  3.  Effect of original and Fe-Al-Zr modified anthracites dosage on adsorption rate of phosphorus

    图  4  Fe-Al-Zr改性无烟煤对磷的吸附动力学曲线拟合

    Figure  4.  Adsorption dynamics of phosphorus onto Fe-Al-Zr modified anthracites

    图  5  Fe-Al-Zr改性无烟煤在不同吸附时间的孔径分布曲线

    Figure  5.  Pore size distribution of Fe-Al-Zr modified anthracites at different time in the adsorption process

    图  6  CaCl2的投加量和溶液pH对磷回收率的影响

    Figure  6.  Effect of CaCl2 dosage and pH on the recovery efficiency of phosphorous

    表  1  无烟煤改性过程中药剂投加量的正交设计

    Table  1.   Orthogonal design of the dosage of reagent in the anthracite modification process

    药剂投加量(mmol/g,以无烟煤计)磷的去
    除率/%
    FeSO4·7H2OFeCl3·6H2OCl2OZr·8H2OAl(NO3)3·9H2O
    122271.35
    124493.37
    244468.79
    244263.87
    下载: 导出CSV

    表  2  Fe-Al-Zr改性无烟煤吸附磷的动力学与等温吸附模型拟合参数

    Table  2.   Fitting parameters of kinetic models and isotherm parameters for the adsorption of phosphorus onto Fe-Al-Zr modified anthracites

    模型模型参数拟合值
    伪一级动力学模型
    ${q_t}{\text{ = } }{q_{\rm{e} } }(1 - { {\rm{e} }^{ - {K_1}t} })$
    K1/(min−1)0.008 6
    qe/(mg/g)3.256
    R20.975 1
    伪二级动力学模型
    $\dfrac{t}{ { {q_t} } } = \dfrac{1}{ { {K_2}q_{\rm{e}}^2} } + \dfrac{t}{ { {q_{\rm{e}}} } }$
    K2/〔g/(mg·min)〕0.006 0
    qe/(mg/g)5.656
    R20.998 8
    Langmuir模型
    ${q_{\rm{e}}} = \dfrac{ { {q_{\rm{m}}}{K_{\rm{L}}}{C_{\rm{e}}} } }{ {1 + {K_{\rm{L}}}{C_{\rm{e}}} } }$
    qm/(mg/g)12.853 0
    KL (L/mg)2.350
    R20.998 3
    Freundlich模型
    ${q_{\rm{e}}} = {K_{\rm{F}}}{C_{\rm{e}}}^{1/n}$
    KF/〔(mg/g)/(mg/L)1/n6.373 0
    1/n2.378
    R20.918 2
    下载: 导出CSV

    表  3  Fe-Al-Zr改性无烟煤吸附磷的颗粒内扩散模型拟合参数

    Table  3.   Fitting parameters of intraparticle diffusion model for the adsorption of phosphorus onto Fe-Al-Zr modified anthracites

    模型参数第一阶段第二阶段
    $ {q}_{t}={K}_{i}{t}^{1/2}+C $Ki/〔mg/(g·min−1/2)〕0.1880.009
    C/(mg/g)2.0125.138
    R20.978 70.648 1
    下载: 导出CSV

    表  4  不同吸附剂除磷性能的比较

    Table  4.   Comparison of phosphorous adsorption of different adsorbent

    吸附剂吸附量/(mg/g)数据来源
    硅改性花生壳生物炭2.79文献[23]
    污泥生物炭9.615文献[24]
    磁性水滑石/生物炭复合材料9.50文献[25]
    微孔碳@粉煤灰复合材料8.375文献[26]
    Fe-Al-Zr改性无烟煤13.022本研究
    下载: 导出CSV

    表  5  Fe-Al-Zr改性无烟煤在4个循环周期中对磷的吸附量和去除率

    Table  5.   Adsorption amount and removal efficiency of Fe-Al-Zr modified anthracites in the four operation cycles

    项目 第1次循环 第2次循环 第3次循环 第4次循环
    第1次吸附 第2次吸附 第3次吸附 第1次吸附 第2次吸附 第1次吸附 第2次吸附 第1次吸附
    吸附量/(mg/g) 6.289 4.181 2.552 4.915 2.139 3.645 1.309 2.778
    去除率/% 96.42 76.53 44.12 76.53 35.28 60.93 22.48 48.03
    下载: 导出CSV
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  • 收稿日期:  2021-07-21

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