A continuous pilot-scale system using coal-mine drainage sludge to treat acid mine drainage contaminated with high concentrations of Pb, Zn, and other heavy metals

被引:38
作者
Cui, Mingcan [3 ,4 ]
Jang, Min [1 ]
Cho, Sang-Hyun [1 ]
Khim, Jeehyeong [4 ]
Cannon, Fred S. [2 ]
机构
[1] Korea Mine Reclamat Corp, Inst Mine Reclamat Technol, Coal Ctr 80 6, Seoul, South Korea
[2] Penn State Univ, Dept Civil & Environm Engn, University Pk, PA 16802 USA
[3] Jilin Inst Chem Technol, Jilin, Peoples R China
[4] Korea Univ, Sch Civil Environm & Architectural Engn, Seoul 136701, South Korea
关键词
Sludge; Acid mine drainage; Heavy metal; Stirring tank reactor; SCHWERTMANNITE; SULFATE; IRON; REMEDIATION; ADSORPTION; ZINC;
D O I
10.1016/j.jhazmat.2012.02.042
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A series of pilot-scale tests were conducted with a continuous system composed of a stirring tank reactor, settling tank, and sand filter. In order to treat acidic drainage from a Pb-Zn mine containing high levels of heavy metals, the potential use of coal-mine drainage sludge (CMDS) was examined. The pilot-scale tests showed that CMDS could effectively neutralize the acidic drainage due to its high alkalinity production. A previous study revealed that calcite and goethite contained in CMDS contributed to dissolutive coprecipitation and complexation with heavy metals. The continuous system not only has high removal efficiencies (97.2-99.8%), but also large total rate constants (K-total, 0.21-10.18 h(-1)) for all heavy metals. More specifically, the pilot system has a much higher Zn(II) loading rate (45.3 g m(-3) day(-1)) than other reference systems, such as aerobic wetland coupled with algal mats and anoxic limestone drains. The optimum conditions were found to be a CMDS loading of 280 g L-1 and a flow rate of 8 L day(-1), and the necessary quantity of CMDS was 91.3 g L-1 day(-1), as the replacement cycle of CMDS was determined to be 70 days. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:122 / 128
页数:7
相关论文
共 27 条
  • [1] Ackman T., 1982, 8672 US BUR MIN
  • [2] [Anonymous], 2006, WORLD HLTH ORG, DOI DOI 10.5942/JAWWA.2017.109.0087
  • [3] Adsorption of Zn(II) from aqueous solution by using different adsorbents
    Bhattacharya, A. K.
    Mandal, S. N.
    Das, S. K.
    [J]. CHEMICAL ENGINEERING JOURNAL, 2006, 123 (1-2) : 43 - 51
  • [4] BIGHAM JM, 1990, GEOCHIM COSMOCHIM AC, V54, P2743
  • [5] Schwertmannite and the chemical modeling of iron in acid sulfate waters
    Bigham, JM
    Schwertmann, U
    Traina, SJ
    Winland, RL
    Wolf, M
    [J]. GEOCHIMICA ET COSMOCHIMICA ACTA, 1996, 60 (12) : 2111 - 2121
  • [6] ON THE INFLUENCE OF CARBONATE IN MINERAL DISSOLUTION .2. THE SOLUBILITY OF FECO3 (S) AT 25-DEGREES-C AND 1 ATM TOTAL PRESSURE
    BRUNO, J
    WERSIN, P
    STUMM, W
    [J]. GEOCHIMICA ET COSMOCHIMICA ACTA, 1992, 56 (03) : 1149 - 1155
  • [7] Electrochemical remediation of acid mine drainage
    Chartrand, MMG
    Bunce, NJ
    [J]. JOURNAL OF APPLIED ELECTROCHEMISTRY, 2003, 33 (3-4) : 259 - 264
  • [8] Geochemical processes controlling fate and transport of arsenic in acid mine drainage (AMD) and natural systems
    Cheng, Hefa
    Hu, Yuanan
    Luo, Jian
    Xu, Bin
    Zhao, Jianfu
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2009, 165 (1-3) : 13 - 26
  • [9] Potential application of sludge produced from coal mine drainage treatment for removing Zn(II) in an aqueous phase
    Cui, Mingcan
    Jang, Min
    Cho, Sang-Hyun
    Khim, Jeehyeong
    [J]. ENVIRONMENTAL GEOCHEMISTRY AND HEALTH, 2011, 33 : 103 - 112
  • [10] Dempsey B.A., 2001, GEOCHEMISTRY-GERMANY, V1, P81, DOI DOI 10.1144/GEOCHEM.1.1.81