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Received April 8, 2018
Accepted June 13, 2018
- 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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Removal of Zn (II) by complexation-ultrafiltration using rotating disk membrane and the shear stability of PAA-Zn complex
School of Chemistry and Chemical Engineering, Central South University, Changsha 410083, China
csu_tian@csu.edu.cn
Korean Journal of Chemical Engineering, October 2018, 35(10), 2078-2085(8), 10.1007/s11814-018-0105-x
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Abstract
Polyacrylic acid sodium (PAAS) was applied to remove Zn (II) from aqueous solutions by complexationultrafiltration using a rotating disk membrane module. As important factors, solution pH and the mass ratio of polymer to metal ions (P/M) on the rejection of Zn (II) were investigated, and the rejection could reach to 95.3% at pH=7, P/M=25 and 500 rpm. In addition, a partition model was proposed to reveal instability mechanism of the PAA-Zn complex in the shear field for the first time. The critical rotating speeds at which PAA-Zn complexes begin to dissociate were 1,460, 1,390, 1,280 rpm at pH 7.0, 6.0, 5.0, respectively. The corresponding critical shear rates (γc), the smallest shear rates at which PAA-Zn complex begins to dissociate, were 1.58 X 10 5, 1.45 X 10 5 and 1.25 X 10 5 s-1 at pH 7.0, 6.0, 5.0, respectively. In addition, the relationship between the critical radii and the critical rotating speed was obtained.
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References
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Kim H, Baek K, Kim BK, Shin HJ, Yang JW, Korean J. Chem. Eng., 25(2), 253 (2008)
Camarillo R, Llanos J, Garcia-Fernandez L, Perez A, Canizares P, Sep. Purif. Technol., 70(3), 320 (2010)
Zhao LM, Zhao HF, Nguyen P, Li AR, Jiang LH, Xia QM, Rong Y, Qiu YJ, Zhou JC, Desalination, 322, 113 (2013)
Zeng JX, Ye HQ, Huang ND, Liu JF, Zheng LF, Chemosphere, 76, 706 (2009)
Buckley LP, Vijayan S, McConeghy GJ, Maves SR, Martin JF, At. Energy Canada Limited, AECL, 90, 1544 (1990)
Hwang KJ, Lin SJ, Chem. Eng. J., 244, 429 (2014)
Hwang KJ, Wu SE, Chem. Eng. Res. Des., 94, 44 (2015)
Hwang KJ, Wang SY, Iritani E, Katagiri N, J. Taiwan Inst. Chem. Eng., 62, 45 (2016)
Zhang WX, Ding LH, Grimi N, Jaffrin MY, Tang B, Sep. Purif. Technol., 175, 365 (2017)
Zhu Z, Mhemdi H, Zhang W, Ding L, Bals O, Jaffrin MY, Grimi N, Vorobiev E, Food Bioprocess Technol., 9, 493 (2016)
Ladeg S, Zhu Z, Moulai-Mostefa N, Ding L, Jaffrin MY, Arab. J. Sci. Eng., 43, 2237 (2018)
Meyer P, Mayer A, Kulozik U, Int. Dairy J., 51, 75 (2015)
Bouzerar R, Jaffrin MY, Ding LH, Paullier P, AIChE J., 46(2), 257 (2000)
Bouzerar R, Ding LH, Jaffrin MY, J. Membr. Sci., 170(1), 127 (2000)
Itoh M, Yamada Y, Imao S, Gonda M, Exp. Therm. Fluid Sci., 5, 359 (1992)
Torras C, Pallares J, Garcia-Valls R, Jaffrin MY, Desalination, 200(1-3), 453 (2006)
de Alvarenga ES, de Oliveira CP, Bellato CR, Carbohydr. Polym., 80, 1155 (2010)
Canizares P, Perez A, Camarillo R, Mazarro R, J. Membr. Sci., 320(1-2), 520 (2008)
Arthanareeswaran G, Thanikaivelan P, Jaya N, Mohan D, Raajenthiren M, J. Hazard. Mater., 139(1), 44 (2007)
Romero-Gonzalez ME, Williams CJ, Gardiner PHE, Environ. Sci. Technol., 35, 3025 (2001)
Jaffrin MY, J. Membr. Sci., 324(1-2), 7 (2008)
Zeng JX, Ye HQ, Hu ZY, J. Hazard. Mater., 161(2-3), 1491 (2009)