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Received August 25, 2013
Accepted October 14, 2013
- 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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Optimization of preparation conditions of polyamide thin film composite membrane for organic solvent nanofiltration
Department of Chemical Engineering, Faculty of Engineering, Ferdowsi University of Mashhad, P. O. Box 9177948974, Mashhad, Iran, Korea
pakizeh@um.ac.ir
Korean Journal of Chemical Engineering, February 2014, 31(2), 327-337(11), 10.1007/s11814-013-0213-6
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Abstract
Separation performance of polyamide composite membranes is affected by several parameters during formation of thin upper layer via interfacial polymerization. We investigated the effect of various polyamide synthesis conditions on the performance of organic solvent resistant polyamide composite membranes through the model equations designed by 2-level fractional factorial design. The dewaxing solvent recovery was selected as separation process. Five factors were changed in two level includin; TMC concentration (0.05-0.1%), MPD concentration (1-2%), support immersion time in organic solution (2-4 min), support immersion time in aqueous solution (1-2 min), and curing temperature (70-80 ℃). The resultant equations showed 93.48% and 94.82% of the variability (R2adj) in data used to fit oil rejection and permeate flux models, respectively. The analysis of variance revealed that both models were high significant. It was also observed that TMC concentration, MPD concentration and immersion time in TMC have more pronounced effect on the oil rejection and permeate flux than other factors and interactions. Optimal polyamide preparation conditions were obtained using multiple response method for 94% oil rejection as target value. According to the results, the best value of permeate flux (8.86 l/(m2·h)) was found at TMC concentration of 0.1%, MPD concentration of 1.94%, immersion time in TMC of 3.88 min, immersion time in MPD of 1.95 min and curing temperature of 71.96 ℃ with desirability factor of 1.
Keywords
References
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Tang CYY, Kwon YN, Leckie JO, Desalination, 242(1-3), 168 (2009)
Kong Y, Shi DQ, Yu HW, Wang YF, Yang JR, Zhang YY, Desalination, 191(1-3), 254 (2006)
Nunes SP, Peinemann KV, Membrane Technology in the Chemical Industry, Wiley-VCH, Weinheim (2001)
Matsuura T, Desalination, 134(1-3), 47 (2001)
Lau WJ, Ismail AF, Misdan N, Kassim MA, Desalination, 287, 190 (2012)
Ghosh AK, Jeong BH, Huang XF, Hoek EMV, J. Membr. Sci., 311(1-2), 34 (2008)
Greenlee LF, Lawler DF, Freeman BD, Marrot B, Moulin P, Water Res., 43, 2317 (2009)
Kong CL, Shintani T, Kamada T, Freger V, Tsuru T, J. Membr. Sci., 384(1-2), 10 (2011)
Kosaraju PB, Sirkar KK, J. Membr. Sci., 321(2), 155 (2008)
Solomon MFJ, Bhole Y, Livingston AG, J. Membr. Sci., 423, 371 (2012)
Solomon MFJ, Gorgojo P, Munoz-Ibanez M, Livingston AG, J. Membr. Sci., In press (2013)
Dalwani M, Benes NE, Bargeman G, Stamatialis D, Wessling M, J. Membr. Sci., 372(1-2), 228 (2011)
Kim IC, Jegal J, Lee KH, J. Polym. Sci. B: Polym. Phys., 40(19), 2151 (2002)
Oh NW, Jegal J, Lee KH, J. Appl. Polym. Sci., 80(14), 2729 (2001)
Singh PS, Joshi SV, Trivedi JJ, Devmurari CV, Rao AP, Ghosh PK, J. Membr. Sci., 278(1-2), 19 (2006)
Ghosh AK, Hoek EMV, J. Membr. Sci., 336(1-2), 140 (2009)
Chen SH, Chang DJ, Liou MR, Hsu CS, Lin SS, J. Appl. Polym. Sci., 83(5), 1112 (2002)
Rao AP, Joshi SV, Trivedi JJ, Devmurari CV, Shah VJ, J. Membr. Sci., 211(1), 13 (2003)
Tang CYY, Kwon YN, Leckie JO, Desalination, 242(1-3), 168 (2009)
Freger V, Langmuir, 19(11), 4791 (2003)
Freger V, Langmuir, 21(5), 1884 (2005)
Montgomery DC, Design and analysis of experiments, John Wiley, New York (1997)
Box GEP, Hunter WG, Hunter JS, Statistics for experimenters-an introduction to design, data analysis and model building, John Wiley & Sons, New York (1978)
Rathinam A, Rao JR, Nair BU, J. Taiwan Inst. Chem. Eng., 42, 952 (2011)
Gottipati R, Mishra S, Chem. Eng. J., 160(1), 99 (2010)
Mirmohseni A, Zavareh S, J. Polym. Res., 17, 191 (2010)
Takht Ravanchi M, Kaghazchi T, Kargari A, Soleimani M, J. Taiwan Inst. Chem. Eng., 40, 511 (2009)
Shokri E, Yegani R, J. Memb. Sep. Technol., 1, 43 (2012)
Abdul-Wahab SA, Abdo J, Appl. Therm. Eng., 27, 413 (2007)
Amirilargani M, Sadrzadeh M, Mohammadi T, J. Polym. Res., 17, 363 (2010)
Li Y, Guan HM, Chung TS, Kulprathipanja S, J. Membr. Sci., 275(1-2), 17 (2006)
Namvar-Mahboub M, Pakizeh M, Sep. Puri. Technol., 119, 35 (2013)
Tang CYY, Kwon YN, Leckie JO, Desalination, 242(1-3), 168 (2009)
Kong Y, Shi DQ, Yu HW, Wang YF, Yang JR, Zhang YY, Desalination, 191(1-3), 254 (2006)