Phase Behavior and Ternary Diagram Construction for Membrane Forming Polycarbonate Solutions

Article Preview

Abstract:

Cloud points at different polymer concentrations were obtained by the simple titration method and compared with the numerically calculated theoretical binodal curves for Polycarbonate/Dimethylacetamide/Water (PC/DMAc/Water) and Polycarbonate/N-Methyl-2-pyrrolidone/Water (PC/NMP/Water). The interaction parameters for solvent polymer and nonsolvent polymer were obtained from Hansen's solubility parameters. The cloud points determined were found to be in close agreement with the theoretical binodal curve calculated. Coagulation values for different solvents such as Dichloromethane (DCM), Dimethylacetamide (DMAc), N-Methyl-2-pyrrolidone (NMP) and Tetrahydrofuran (THF) were also determined and the results were plotted in a ternary diagram to realize the effect of interaction parameters on the coagulation values. The higher the mutual affinity of solvent to polymer (low χ23), the faster is the liquid-liquid demixing rate to occur. For DCM solvent, fastest demixing rate was exhibited and lowest for the THF.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

7-10

Citation:

Online since:

September 2014

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2014 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] Jong Hak, K., et al., Phase behavior and mechanism of membrane formation for polyimide/DMSO/water system. J. Membrane Sci. 2001. 187.

Google Scholar

[2] Strathmann, H. and K. Kock, The formation mechanism of phase inversion membranes. Desalination, (1977).

DOI: 10.1016/s0011-9164(00)88244-2

Google Scholar

[3] Machado, P.S.T., A.C. Habert, and C.P. Borges, Membrane formation mechanism based on precipitation kinetics and membrane morphology: flat and hollow fiber polysulfone membranes. J. Membrane Sci. 1999. 155.

DOI: 10.1016/s0376-7388(98)00266-x

Google Scholar

[4] Ian, H. and M. Matthew, Phase Separation in Ternary Polymer Solutions Induced by Solvent Loss. Macromolecules, 2002. 35.

Google Scholar

[5] Marco Di, L., N. Ronaldo, and P.B. Cristiano, Microporous anisotropic phase inversion membranes from bisphenol A polycarbonate: Effect of additives to the polymer solution. J. Appl. Polym. Sci. 2002. 86.

DOI: 10.1002/app.11338

Google Scholar

[6] Juin-Yih, L., et al., Construction of ternary phase diagrams in nonsolvent/solvent/PMMA systems. J. Polym. Sci. Pol. Phys., 1998. 36.

Google Scholar

[7] Hansen, C.M., Hansen Solubility Parameters. A User's Handbook, , 2000, CRC Press: Boca Raton.

Google Scholar

[8] Pesek, S.C. and W.J. Koros, Aqueous quenched asymmetric polysulfone membranes prepared by dry/wet phase separation. J. Membrane Sci., 1993. 81.

DOI: 10.1016/0376-7388(93)85032-r

Google Scholar

[9] Zeman, L. and G. Tkacik, Thermodynamic analysis of a membrane-forming system water/N-methyl-2-pyrrolidone/polyethersulfone. J. Membrane Sci., (1988).

DOI: 10.1016/0376-7388(88)80011-5

Google Scholar

[10] Yilmaz, L. and A.J. McHugh, Analysis of nonsolvent–solvent–polymer phase diagrams and their relevance to membrane formation modeling. J. Appl. Polym. Sci, 1986. 31.

DOI: 10.1002/app.1986.070310837

Google Scholar

[11] Frank, W.A. and C.A. Smolders, Calculation of liquid-liquid phase separation in a ternary system of a polymer in a mixture of a solvent and a nonsolvent. Macromolecules, 1982. 15.

DOI: 10.1021/ma00234a008

Google Scholar

[12] Yong-Ming, W., et al., Mathematical calculation of binodal curves of a polymer/solvent/nonsolvent system in the phase inversion process. Desalination, 2006. 192.

DOI: 10.1016/j.desal.2005.07.035

Google Scholar

[13] Barzin, J. and B. Sadatnia, Theoretical phase diagram calculation and membrane morphology evaluation for water/solvent/polyethersulfone systems. Polymer, 2007. 48.

DOI: 10.1016/j.polymer.2007.01.049

Google Scholar

[14] Dongliang, W., et al., Phase separation phenomena of polysulfone/solvent/organic nonsolvent and polyethersulfone/solvent/organic nonsolvent systems. J. Appl. Polym. Sci., 1993. 50.

DOI: 10.1002/app.1993.070501003

Google Scholar

[15] Thomas, L., L.M. Michael, and M.K. Georgios, A Flory–Huggins model based on the Hansen solubility parameters. Fluid Phase Equilibr, 2002. 203.

Google Scholar