Abstract
In order to investigate the effects of the non-solvent species on the formation mechanism of polyacrylonitrile (PAN) fiber in wet spinning, theoretical ternary phase diagrams of water/DMSO/PAN and ethanol/DMSO/PAN systems were constructed based on the extended Flory–Huggins theory. The cloud-points of dilute PAN solutions of the two systems were determined by titration method and those of concentrated PAN solutions from Boom’s linearized cloud-point correlation. Binary interaction parameters were calculated and optimized to construct the theoretical phase diagram. The obtained diagrams were used to investigate the effects of the non-solvent species on the formation of PAN fibers. If the non-solvent water is replaced with ethanol, the meta-stable two-phase region in the ternary phase diagram increases. This favors the de-mixing of the filament via nucleation and growth mechanism during the coagulation process, resulting in homogenous dense PAN fibers with low porosity.
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Abbreviations
- a, b, a 0, a 1, a 2, a 3, a 4, α:
-
Constants
- w 1 :
-
Mass fraction of non-solvent
- w 2 :
-
Mass fraction of solvent
- w 3 :
-
Mass fraction of polymer
- g 12 :
-
Concentration-dependent binary interaction parameter between non-solvent and solvent
- g 23 :
-
Binary interaction parameter between solvent and polymer
- g 13 :
-
Binary interaction parameter between non-solvent and polymer
- ΔG m :
-
Gibbs free energy of mixing
- ΔG E :
-
Excess Gibbs free energy of mixing
- n 1 :
-
Molar fraction of non-solvent
- n 2 :
-
Molar fraction of solvent
- R :
-
Gas constant
- T :
-
Absolute temperature
- Λ12, Λ21 :
-
Wilson parameter
- ϕ1 :
-
Volume fraction of non-solvent
- ϕ2 :
-
Volume fraction of solvent
- ϕ3 :
-
Volume fraction of polymer
- V 1 :
-
Molar volume of non-solvent
- V 2 :
-
Molar volume of solvent
- λ12 = λ21 :
-
Interaction energy parameter between non-solvent and solvent
- λ22 :
-
Interaction energy parameter between solvent and solvent
- λ11 :
-
Interaction energy parameter between non-solvent and non-solvent
- γ1 :
-
Activity coefficient of non-solvent
- γ2 :
-
Activity coefficient of solvent
- δ1,d :
-
Dispersion force component of the solubility parameter of non-solvent
- δ1,p :
-
Polar force component of the solubility parameter of non-solvent
- δ1,h :
-
Hydrogen bond component of the solubility parameter of non-solvent
- δ3,d :
-
Dispersion force component of the solubility parameter of polymer
- δ3,p :
-
Polar force component of the solubility parameter of polymer
- δ3,h :
-
Hydrogen bond component of the solubility parameter of polymer
- Δμ1 :
-
Difference between the chemical potential of non-solvent in the mixture and the pure state
- Δμ2 :
-
Difference between the chemical potential of solvent in the mixture and the pure state
- Δμ3 :
-
Difference between the chemical potential of polymer in the mixture and the pure state
- Δμ1,A :
-
Difference between the chemical potential of non-solvent in polymer-rich phase and the pure state
- Δμ2,A :
-
Difference between the chemical potential of solvent in polymer-rich phase and the pure state
- Δμ3,A :
-
Difference between the chemical potential of polymer in polymer-rich phase and the pure state
- Δμ1,B :
-
Difference between the chemical potential of non-solvent in polymer-poor phase and the pure state
- Δμ2,B :
-
Difference between the chemical potential of solvent in polymer-poor phase and the pure state
- Δμ3,B :
-
Difference between the chemical potential of polymer in polymer-poor phase and the pure state
- ϕ1,A :
-
Volume fraction of non-solvent in polymer-rich phase
- ϕ2,A :
-
Volume fraction of solvent in polymer-rich phase
- ϕ3,A :
-
Volume fraction of polymer in polymer-rich phase
- ϕ1,B :
-
Volume fraction of non-solvent in polymer-poor phase
- ϕ2,B :
-
Volume fraction of solvent in polymer-poor phase
- ϕ3,B :
-
Volume fraction of polymer in polymer-poor phase
- \( G_{22} \) :
-
\( \frac{{\partial^{2} \Updelta G_{\text{m}} }}{{\partial (\phi_{2} )^{2} }} \)
- \( G_{33} \) :
-
\( \frac{{\partial^{2} \Updelta G_{\text{m}} }}{{\partial (\phi_{3} )^{2} }} \)
- \( G_{23} \) :
-
\( \frac{{\partial^{2} \Updelta G_{\text{m}} }}{{\partial \phi_{2} \partial \phi_{3} }} \)
- \( G_{222} \) :
-
\( \frac{{\partial^{3} \Updelta G_{\text{m}} }}{{\partial (\phi_{2} )^{3} }} \)
- \( G_{223} \) :
-
\( \frac{{\partial^{3} \Updelta G_{\text{m}} }}{{\partial (\phi_{2} )^{2} \partial \phi_{3} }} \)
- \( G_{233} \) :
-
\( \frac{{\partial^{3} \Updelta G_{\text{m}} }}{{\partial \phi_{2} \partial (\phi_{3} )^{2} }} \)
- u 1 :
-
ϕ1/(ϕ1 + ϕ2)
- u 2 :
-
ϕ2/(ϕ1 + ϕ2)
- PAN:
-
Polyacrylonitrile
- DMSO:
-
Dimethyl sulfoxide
- LCP:
-
Linearized cloud-point
- NG:
-
Nucleation and growth
- SD:
-
Spinodal decomposition
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Acknowledgments
The authors gratefully acknowledge the financial support from the Science and Technology Commission of Shanghai Municipality (07QA14001) and National 973 Project (2006CB605302 and 2006CB605303).
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Zhang, J., Zhang, Y. & Zhao, J. Thermodynamic study of non-solvent/dimethyl sulfoxide/polyacrylonitrile ternary systems: effects of the non-solvent species. Polym. Bull. 67, 1073–1089 (2011). https://doi.org/10.1007/s00289-011-0525-9
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DOI: https://doi.org/10.1007/s00289-011-0525-9