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. 2025 Apr 4;17(7):984.
doi: 10.3390/polym17070984.

Effect of Choline Chloride-Based DES on the Pore-Forming Ability and Properties of PVDF Membranes Prepared with Triethyl Phosphate as Green Solvent

Affiliations

Effect of Choline Chloride-Based DES on the Pore-Forming Ability and Properties of PVDF Membranes Prepared with Triethyl Phosphate as Green Solvent

Alejandro Gálvez-Subiela et al. Polymers (Basel). .

Abstract

This study explores the influence of various additives on the morphological, chemical, and thermal properties of poly(vinylidene fluoride) (PVDF) membranes prepared via the non-solvent induced phase separation (NIPS) technique. The use of a green solvent such as triethyl phosphate (TEP) was shown to be successful. A particular focus was dedicated to pore formers based on choline chloride-based deep eutectic solvents (DES) in combination with ethylene glycol and glycerol, i.e., ChCl/EG and ChCl/GLY, and its benchmark with traditional counterparts such as poly(ethylene glycol) (PEG) and glycerol (GLY). Comprehensive characterization was conducted using FESEM, FTIR, XRD, and DSC techniques to evaluate changes in membrane morphology, porosity, and crystallinity. PEG acted as a pore-forming agent, transitioning the internal structure from spherulitic to sponge-like with consistent pore sizes, while GLY produced a nodular morphology at higher concentrations due to increased dope solution viscosity. DES induced significant shifts in crystalline phase composition, decreasing α-phase fractions and promoting β-phase formation at higher concentrations. While the overall porosity remained unaffected by the addition of GLY or PEG, it was dependent on the DES concentration in the dope at lower values than those obtained by GLY and PEG. Membrane pore size with ChCl/GLY was lower than with ChCl/EG and GLY. All membranes showed performance at the hydrophobic regime. The findings demonstrate that ChCl/EG and ChCl/GLY can tailor the structural and thermal properties of TEP-driven PVDF membranes, providing a green and versatile approach to customize the membrane properties for specific applications.

Keywords: choline chloride; deep eutectic solvent (DES); glycerol; green solvent; membrane; non-solvent induced phase separation (NIPS); poly(vinylidene fluoride) PVDF; polyethylene glycol (PEG); triethyl phosphate (TEP).

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Conflict of interest statement

The authors declare no conflicts of interest.

Figures

Figure 1
Figure 1
FTIR spectra for wavenumbers between 1500 and 500 cm−1 of the elaborated membranes with different additives at 5.00 wt%: (a) pristine PVDF membrane; (b) poly(ethylene glycol) (PEG); (c) choline chloride/ethylene glycol (1:2) DES (ChCl/EG); (d) glycerol (GLY); (e) choline chloride/glycerol (1:2) DES (ChCl/GLY). Peaks associated with α-crystalline phase bonds are in dashed lines, while the solid lines refer to β-crystalline phases.
Figure 2
Figure 2
FTIR spectra between 1500 and 500 cm−1 of the membranes with addition of (a) choline chloride/ethylene glycol (1:2) DES (ChCl/EG) and (b) choline chloride/glycerol (1:2) DES (ChCl/GLY) at different concentrations (wt%).
Figure 3
Figure 3
XRD diffractogram of the membranes with the different additives at 5.00 wt%: poly(ethylene glycol) (PEG); choline chloride/ethylene glycol (1:2) DES (ChCl/EG); glycerol (GLY); choline chloride/glycerol (1:2) DES (ChCl/GLY).
Figure 4
Figure 4
DSC melting process analysis of the membranes with the different additives at 5.0 wt%: poly(ethylene glycol) (PEG); choline chloride/ethylene glycol (1:2) DES (ChCl/EG); glycerol (GLY); choline chloride/glycerol (1:2) DES (ChCl/GLY).
Figure 5
Figure 5
DSC melting process analysis of the pristine PVDF membrane and with different concentrations (wt%) of (a) choline chloride/ethylene glycol (1:2) DES (ChCl/EG) and (b) choline chloride/glycerol (1:2) DES (ChCl/GLY).

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