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Received October 29, 2019
Accepted February 6, 2020
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Selective separation of Cd(II), Zn(II) and Pb(II) from Pb-Zn smelter wastewater via shear induced dissociation coupling with ultrafiltration
School of Chemistry and Chemical Engineering, Central South University, Changsha 410083, China
csu_tian@csu.edu.cn
Korean Journal of Chemical Engineering, May 2020, 37(5), 784-791(8), 10.1007/s11814-020-0509-2
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Abstract
Treatment of Pb-Zn smelter wastewater via complexation-ultrafiltration (C-UF) was studied using copolymer of acrylic acid-maleic acid (PMA) as complexant. The complexing reaction kinetics of M (Cd(II), Pb(II) and Zn(II)) with PMA were examined for the first time and the pseudo-first-order model could be employed to simulate the reaction. The effects of the mass ratio of PMA to metal ions (P/M) and pH on the simultaneous removal of Cd(II), Zn(II) and Pb(II) via C-UF were investigated, and the optimized P/M and pH are 10 and 7.0, respectively. Furthermore, the shear stability of PMA-Cd, PMA-Zn and PMA-Pb complexes was investigated, and the corresponding critical shear rates (γc), the smallest shear rate at which the complexes begin to dissociate were 1.98 X 105, 1.81 X 104 and 1.38 X 105 s-1, respectively. The selective recovery of Cd(II), Zn(II) and Pb(II) from Pb-Zn Smelter wastewater as well as the regeneration of PMA were fulfilled by shear induced dissociation coupled with ultrafiltration (SID-UF) according to the difference of critical shear rates of PMA-M complexes, and the regenerated PMA showed almost the same complexation ability as the original.
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References
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Zeng JX, Ye HQ, Hu ZY, J. Hazard. Mater., 161(2-3), 1491 (2009)
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Evina K, Simos M, Haralambous KJ, Chemosphere, 82, 557 (2011)
Huang YF, Wu DH, Wang XD, Huang W, Lawless D, Feng XS, Sep. Purif. Technol., 158, 124 (2016)
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Khosa MA, Shah SS, Feng XS, Chem. Eng. J., 244, 446 (2014)
Llanos J, Perez A, Rodrigo MA, Canizares P, J. Hazard. Mater., 168(1), 25 (2009)
Le HS, Qiu YR, Tang SY, Desal. Water Treat., 160, 41 (2019)
Camarillo R, Perez A, Canizares P, de Lucas A, Desalination, 286, 193 (2012)
Tang SY, Qiu TR, Korean J. Chem. Eng., 36(8), 1321 (2019)
Zhang Q, Gao J, Qiu YR, Chem. Eng. Process., 135, 236 (2019)
Xu JY, Tang SY, Qiu YR, J. Cent. South Univ., 26, 577 (2019)
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Gull P, Malik MA, Dar OA, Hashmi AA, J. Mol. Struct., 1134, 734 (2017)
Llanos J, Camarillo R, Perez A, Canizares P, Sep. Purif. Technol., 73(2), 126 (2010)
Canizares P, Perez A, Camarillo R, Mazarro R, J. Membr. Sci., 320(1-2), 520 (2008)
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Bouzerar R, Jaffrin MY, Ding LH, Paullier P, AIChE J., 46(2), 257 (2000)
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