Electrospinning of PVDF literature summary.
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Open access peer-reviewed chapter
By Dinesh Lolla, Lin Pan, Harshal Gade and George G. Chase
Submitted: October 2nd 2017Reviewed: March 6th 2018Published: September 12th 2018
Electrospun polymeric nanofibers with flexible three-dimensional porous structures and high surface-to-volume ratio are potential resources for several novel applications in the fields of micro- and nanoscale filtration, water desalination, drug delivery, life sciences, catalysis, and energy harvesters. Functionalized polymeric fibers with enhanced molecular orientation, surface textural morphologies, and piezo-, pyro-, and ferroelectric properties are of technical and commercial interest around the world. Several emerging technologies including electrical polarization, vacuum plasma treatment, corona discharge, surface fluorination, and chemical treatments to functionalize the polyvinylidene fluoride nanofibers are discussed as potential applications of electroactive materials.
Polyvinylidene fluoride (PVDF) is a semicrystalline, dielectric polymer with very high breakdown strength that offers long-duration surface charge retention, due to its unique dipole molecular structure with CH2-CF2 repeated monomer units . PVDF is regarded as one of the most suitable polymeric materials to study polarizability in dielectric polymers. The dipole monomer structure of PVDF is favored in converting electromechanical coupling behavior with variance in thermomechanical processing. Although the piezoelectric coefficient of PVDF and its copolymers PVDF-HFP and PVDF-TrFE are less than piezoelectric ceramics like PBZ and BaTiO3, their elasticity and mechanical stretchability make them more reliable materials for several emerging applications . Moreover, PVDF exhibits higher piezoelectric response voltage, good thermal stability, and chemical resistance suitable for sensors, aerosol filters, actuators, fuel cells, energy harvesters, and other applications [3, 4, 5, 6, 7].
Depending on the crystalline conformations, PVDF exhibits five different molecular morphologies labeled as α, β, γ, δ, and ε. The composition and distinctive character of individual and binary phases are studied using Fourier transform infrared spectrometry (FTIR) and X-ray diffractometry (XRD) analysis. The α-phase consists of a non-centrosymmetric crystal structure with CH2-CF2 dipoles oriented in the same direction and has an all-trans (TTTT) planar zigzag conformation . The β-phase follows a trans-gauche-trans-gauche’ (TGTG’) atomic arrangement of a centrosymmetric unit cell. In this atomic configuration, the CH2 dipoles are perpendicular to CF2 repeat units, and this produces a permanent electric dipole perpendicular to the axis with corresponding strong and ferroelectric and piezoelectric charges. The γ-phase has T3GT3G’ conformations where the CH2-CF2 dipoles are oriented parallel to each other to form a non-centrosymmetric polar crystal. In general, the γ- and δ-phases form as a result of high-pressure crystallization [8, 9], are not commonly observed in the electrospun fibers, and hence are not considered further here.
Phase transformations among the crystal orientations take place under various postprocessing such as heat treatment, uniaxial stretching, and electrical poling [9, 10, 11]. Phase transformational mechanisms caused by polarization are interpreted in terms of vibrational motions around the individual atomic bonds in the PVDF molecule. Two distinct motions, known as flip-flop (segmental) and inversion motions (macromolecular), were observed during transformation of phases in polarization treatments. The segmental flip-flop motions usually occur at about 150°C (the Curie temperature) and result in a gradual change in the molecular conformations. Higher temperatures above 170°C are usually needed to produce inversion motions but can be achieved near the Curie temperature by subjecting the PVDF fibers with simultaneous electromechanical effects. Heat treatment in the presence of high electric fields and elevated ambient pressures can produce transformations from α- to β-phase and β- to γ-phase (<280°C, <4000 atm). The reverse transformations from β- to α-phase and γ- to α-phase typically require higher temperature and pressure (>290°C, >4500 atm). The transformation from β- to α-phase has so far only been studied in the unoriented state. The γ-phase PVDF melting temperature is about 15°C higher than the α- and β-phase materials. In this chapter, we reported several phase conversion techniques with primary focus on enhancing the amount of β-phase in PVDF fibers using different functionalization routes.
Electrospinning is well documented and is considered an easy laboratory method for producing submicron and nanofibers [12, 13]. Electrospun polymer fibers are widely used in filtration [14, 15], catalysis [16, 17, 18, 19, 20, 21, 22], biomedical materials [23, 24, 25, 26], and electrolytes [7, 27].
The application of electrical forces to produce polymer filaments began in the early 1930s. A brief summary of the early electrospinning literature is provided by Huang et al. . A highly cited reference describing the mechanisms of electrospinning is by Reneker et al. .
The electrospinning process is driven by the electrical forces on the surface or inside the polymer solution. The free charges (ions) inside the polymer solution move in response to the electrical field and transfer a force to the solution . When the electrically induced forces exceed the surface tension force, a liquid jet is ejected from the surface .
A schematic diagram of a typical laboratory electrospinning setup is shown in Figure 1. The components are high-voltage power supply, a syringe pump that delivers polymer solution through a tube to a small diameter needle, and a grounded rotating drum collector surface. The high voltage creates the electrical charge in the solution, and a jet is driven by the potential between the needle and the collector. As the jet travels to the collector, the solvent evaporates, and the jet solidifies into small fibers that deposit on the collector surface.
Many natural and synthetic polymers have been electrospun to produce fine fibers, such as polyacrylonitrile (PAN), polyvinyl alcohol (PVA), poly(methyl methacrylate) (PMMA), polyethylene oxide (PEO), polyethylene (PE), and polypropylene (PP) . In comparison, PVDF has attracted much attention due to its properties and molecular structure. Table 1 summarizes solution and spinning conditions for electrospinning PVDF fibers reported in literature. In addition, some researchers have modified the properties of the PVDF fiber mats by blending with other polymers . As an example Gopalan et al.  mixed PVDF with varying amounts of PAN to fabricate fiber mats for use in lithium batteries. Ding and coworkers mixed PVDF with PMMA for same purpose, Guo et al.  prepared the PU/PVDF electrospun scaffolds for wound healing, and Dong et al.  electrospun PVDF/PTFE membranes for distillation.
|MW||Conc. (%)||Solvent||Electrospun gap (volts)||Application||Ref.|
|107 K||20||DMF:DMA (1:1)||20 cm, 20 kV||Flat ribbons|||
|25||DMA||15 cm, 10 kV||Electrolyte or separator|||
|107 K||DMF:Ac (7:3) (v:v)||20 cm, 25 kV||Batteries|||
|15||DMF:Ac (2:8) (v:v)||8–15 kV||Metal cells|||
|DMF:Ac (6:4) (w:w)||12 cm, 25 kV|
15 cm, 28 kV
|20||DMF:Ac (7:3) (w:w)||15 cm, 25 kV||Separator|||
|14–24||DMF:Ac (3:7, 4:6, 5:5, 6:4, 7:3)||15 cm, 15–18 kV||Filtration|||
|16–20||DMS:Ac (1:1)||10–16 kV||Energy harvester|||
|DMF water (50:3) (w:w)||40 cm, 22.5 kV||Electrode|||
Properties of nanofibers, such as electrical, textural, optical, adhesive, and tensile strength, are highly dependent on the inherent polymeric properties and internal molecular structure. The chemical modification of polymer nanofibers introduces new characteristics to the materials that extend and enhance the scope of their industrial applications over several orders of magnitude. Hence, enhancement of molecular orientation of the PVDF nanofibers has attracted interest of the scientific community. A number of functionalization techniques are available in pilot and commercial scale operations. These functionalization processes can be economical, profitable, environmentally friendly, and long-term reliable [44, 45].
Fiber stretching during the electrospinning process causes dipoles to align perpendicular relative to each other . Piezoresponse force microscopy (PFM) was used to analyze piezoelectric responses and ferroelectric domains in individual electrospun nanofibers with diameters 70, 170, and 400 nm . The β-phase compositions of individual fibers were estimated in the 80–87% range using Beer-Lambert’s law, confirming that fibers with smaller diameters experienced higher oriented conformational changes consistent with stronger elongational forces such as those produced with near-field electrospinning (NFES) due to short tip to collector distances.
Liu et al.  studied processing and solution conditions to obtain the highest β-content when PVDF was electrospun together with multiwalled carbon nanotubes (MWCNTs). Distinct oriented crystalline structures of the MWCNT/PVDF in aligned nanofibers were obtained. Due to the nucleation of highly oriented fibers and extended molecular crystallites at the interface, NFES techniques showed 28% increase in β-phase with 0.05% wt% of MWCNTs.
Served et al.  subjected a pre-stretched 100-μm-thick PVDF film containing exclusively α-phase with 5% head-to-head- and tail-to-tail-type (HHTT) defects to electrical poling at 80 and 170°C (Tm-178°C). Aluminum electrodes were placed on either side of the film, and a DC electric field of 1 MV/cm was used for charging. At 170°C the film changed from nonpolar α-phase to polar β-phase with TGTG molecular conformations. The β-phase polarized films showed a strong piezoelectric coefficient, d33 = 8.5pC/N, and was validated with XRD and FTIR analysis. Salimi et al.  analyzed β-content in compression-molded PVDF films made of two different grades of raw polymer (Kynar® 720, Hylar® MP10). A maximum of 74% β-phase was observed for films that were 38–40% crystalline at 90°C and stretched at a ratio between 4.5 and 5. A similar study of nanoscale domain imaging and spatial distribution of d33 on single electrospun fibers concluded that the d33 distribution was more uniform along the length of the fibers compared to cross-sectional diameter .
Real-time piezoelectric responses were observed by manipulating the operational voltages of a PFM at a spring constant of 0.11 Nm−1, with cantilever resonating frequency of 135 kHz and the amplitude changing stepwise from −30 to +30 V. The highest deflection in the piezoresponse hysteresis loop at 3.3 nm was observed at a Vdc of -30 V. XRD patterns decrypted using a curve deconvolution technique revealed 72.7% β-phase at plane (110,200) and 15.1% α-phase (202) and indicated voltages as much as ±30 V can cause significant effects on nanoscale β-phase nanocrystals. Nanodomains were distributed along to the fiber axis, and the β-phase orientation was investigated by TEM and XRD . Furthermore, polymer composites can be polarized at low electric field strengths with addition of nanoparticle ferroelectric ceramics [49, 50].
Introduction of chemical functional groups into virgin PVDF polymer has resulted in novel functional characteristics [51, 52]. Several studies have reported the ability of modifying structural morphologies and analytical properties in electrospun PVDF nanofibers via plasma deposition of polymers under inert conditions. Molecular cross-linking on PVDF can be achieved through dehydrofluorination or by introducing functional comonomers during electrospinning [5, 8, 53].
The PVDF materials with modified properties are of significant practical interest. In filtration, for example, an exceptional particle capture efficiency of ≥99.999% was achieved by a hybrid monolithic electret aerogel composed of syndiotactic polystyrene (sPS)/PVDF , whereas 98.9% filtration efficiency was recorded with sPS monolithic aerogel comprised of similar solid content. In comparison, performance of cellulose acetate electrospun fibers with diameters in the range from 0.1 to 24 μm challenged with a solid brine aerosol (NaCl) and a liquid aerosol of (diethyl hexyl sebacate) showed a maximum efficiency of 70% and with the most penetrating particle size in the range of 40–270 nm .
Electrospinning solutions 10 wt% were prepared by dissolving Kynar® 761 grade resin (MW of about 550,000, melt viscosity of 35 kp, and a solution viscosity of 350cp at room temperature), PVDF powder (Arkema Inc., USA) in cosolvents N-N-dimethylformamide (DMF), and acetone (Sigma-Aldrich, USA). The solutions were electrospun under the conditions reported in Table 2.
|Conc. PVDF (wt%)||DMF:acetone (w:w)||Gap distance (cm)||Voltage (kV)||Flow rate (mL/h)||Collector rotation (RPM)||Avg. fiber dia. (nm)||Standard deviation (nm)|
Mats of 20 g/m2 basis weight were preheated in an oven at 70°C for 4 hrs before any analysis. Fiber morphologies were analyzed under a scanning electron microscope. Smooth and consistent fibers were observed as shown in Figure 2. A maximum of 57.7% β-content in the fibers was observed. SEM images occasionally showed branched fibers. Branched fibers were formed because of “static equilibrium undulations under the combined effect of the electric Maxwell stresses and surface tension as the electrical stresses are increased” .
A segment of 8X5nm PVDF fiber was studied under an aberration-corrected electron microscope with highly controlled electron beam shown in Figure 3. The images revealed the paths of individual monomers aligned in the direction of fiber axis as shown in Figure 3A. CF2 bonds appeared as brighter dots compared to other bonds as gray and black dots. The raw TEM micrograph was converted into a Fourier transform image to reduce the electron noise and reverted as an RGB image to enhance the features. Paths of CF2 molecules from end to end are clearly seen in the enhanced RBG image in Figure 3B. The calculated distance between the centers of two adjacent bright dots in Figure 3B is about 0.25 nm which is consistent with molecular dynamic simulation of the theoretical distance between fluorine atoms in the β-phase crystallographic structure of the PVDF  in Figure 3C.
Lolla et al.  describe a thermal-stretch-electric field polarization treatment of PVDF nanofibers to fabricate polarized PVDF fiber mats. Simultaneous thermal and electrical treatments caused substantial changes in surface textural morphology. These surface morphological changes are obvious when as-spun fibers shown in Figure 4A are compared to the thermal-electrically treated fibers in Figure 4B.
Surface modifications were found to have a remarkable effect during liquid–liquid filtration applications compared to aerosol filtration as the interfacial strength between liquid droplets is much higher in polarized fiber mats compared to relatively smooth fibers. Kinetic energy generated by electron collision during charge migration is suspected to be the primary reason for surface irregularities. SEM analysis provided only 2D visual conformation of polarization-associated surface modifications. A complete three-dimensional analysis was done to obtain precise increase in roughness due to electron interaction. Lasers were projected in z-direction with the fibers across a 20×30×25μm sample, and few thousands of data points were gathered from hundreds of fibers to make the analysis. All the fiber samples were highly irregular with several mounds, hills, and valley-like structures as shown in Figure 4C and D. Unlike the 2D SEM images, the detailed layer-by-layer fiber interactions were seen, and paths of fiber conglutination or fiber cross-linking were more accurately captured in several directions using laser projections.
2D images of laser intensities were obtained in parallel with three-dimensional images, and an empirical analysis was conducted to estimate the changes in surface morphology. As-spun fibers and thermal-electric treated fibers are shown in Figure 5A and B. The data analysis was conducted on the circular areas highlighted in the images. The radii of the circles in both images were 40 μm. The average intensities of as-spun fibers from peak to valley detection were mapped as shown in Figure 5C represented by the blue line, which gave us a mean surface roughness of Rms = 7.86 ± 4.73 nm. Similar calculations were also performed on the thermal-electric treated fibers, and the mean surface roughness Rms of 16.86 ± 6.68 nm was determined which proves a substantial rise in surface roughness. Average values of roughness averaged over the length of the circumference of circles of varying radius from 0 to 40 μm was used to make a comparison between as-spun and polarized fibers.
Functionalized electrospun fibers are of great interest in aerosol filtration . Fiber mats were subjected to aerosols of 10–250 nm diameter NaCl particles using a TSI-automated filter tester (TSI 8130). Each test was conducted for a duration of 10 s at 10 l/min volumetric flowrate. Three individual samples were consecutively tested 30 times with 30 days between tests to generate a particle capture v/s pressure buildup profile. For thermal-electrically treated polarized fiber mats, the first tests were performed within 24 h of polarization. Both the as-spun and polarized samples showed very distinct and diverse capture trends as apparent from Figure 6A and B. Further research with these materials and with theoretical predictions is needed to explore and understand the shelf life of the filter media in association with net charge. The polarized fibers did not exhibit cake formation, even for the smallest fiber diameters, and had much smaller pressure drop compared to the as-spun fibers. Almost all of the aerosol particles were evenly distributed among individual fibers in the polarized mat as compared to the agglomerates observed in the mat of as-spun fibers.
The plots in Figure 7A show the filter efficiency and pressure drop as a function of the number of tests. Effectively, the plot shows the filter performance over time as it was affected by loading of particles and by charge dissipation (if dissipation occurs) over an extended time. Both the as-spun and polarized filters recorded similar efficiencies of 94.63 ± 012 and 94.96 ± 0.46 during the first experimental run with pressure drops of 56 ± 1.63 and 49.66 ± 1.69 mmH2O, respectively. Pressure drops across the media are in good agreement with the air permeability as shown in Figure 7B.
The Frasier air permeabilities of the fiber mats were tested at two different test pressures at 125 and 2000 kPa. The Darcy law permeability has units of area, whereas the Frazier permeability is reported as volumetric flow rate (cfm = cubic feet per minute). The Darcy permeability can be calculated, but for the purposes here, the relative magnitudes of the two flow rates are the relevant data. The plot in Figure 7B shows that the relative flow rates of the polarized mats were about 17% greater than the flow rates of the as-spun mats, which corresponds to about 17% greater Darcy permeabilities in the polarized mats.
The pressure of 2000 psi is 16 times the pressure drop of 125. If the Darcy permeability was constant, then one would expect the flow rate to increase by a factor of 16 as the pressure increased. The data show that an increase of flow rate was only on order of a factor of 8 times. This indicates that as the flow rate increased the fiber mat structures may have deformed and caused a higher resistance to flow. This topic needs future investigation.
Inspection of SEM images showed attraction between fibers in the polarized mat that caused the fibers to rearrange relative to each other in the fiber mat which resulted in larger pores than the pores in the as-spun mat and is a likely cause of the increase in permeability of the polarized mats. At the end of the 30 filtration experiments, a slight increase in efficiency due to particle accumulation was observed in both the samples. The as-spun fiber mats had a maximum efficiency of 96% at 64 mmH2O pressure drop, and the polarized fibers had a maximum efficiency of 97% pressure drop of 58 mmH2O. Because both efficiencies were very similar, the significant advantage of the polarized mats was the reduced pressure drop.
Population growth, industrialization, rise in living standards, and rapid climate changes have an increased demand for water significantly . Water desalination and purification are a possible solution for providing fresh drinking water to the world especially in drought-prone regions . Researchers have developed several treatment processes such as reverse osmosis (RO), nanofiltration (NF), ultrafiltration (UF), and thermal methods such as membrane distillation to improve water quality and supply. These techniques are energy intensive and have high operating and maintenance costs which make it difficult for developing countries to implement . Membrane distillation finds limited application due to lack of a variety of membranes that can produce stable and high flux for a long time .
Industrial effluents contain a wide range of hazardous and toxic substances including heavy metal ions (Cd2+, Pb2+, Hg2+, Zn2+, etc.), organic acids, nitro compounds, hydrocarbons, sulfides (S2−), sulfites (SO32−), and sugars. Heavy metal pollution can cause serious environmental and health problems to humans . Various methods used for heavy metal removal include ion exchange, electrodialysis, chemical precipitation, and solid-phase extraction [62, 63, 64]. Materials such as nanoparticles, polymers, and organic and inorganic compounds have been employed in the form of thin films, membranes, or powder for water treatment . Apart from these, using a nano-adsorbent for heavy metal removal via adsorption mechanisms is a growing area of research because of its large surface area and mechanical strength . However, regeneration of nano-adsorbents after water treatment is a challenge as adsorption activity decreases with time due to agglomeration. To overcome this challenge, nano-adsorbents can be modified using functionalization techniques .
Blending PVDF with inorganic materials such as ZrO2 , ZnO , Al2O3 , Fe3O4 , CdS , SiO2 , and TiO2  to increase adsorption capacity can help in heavy metal ion removal. This research area is of growing interest. For example, Zhang et al.  used ZnO-hybridized (PVDF/ZnO) membranes for adsorption and desorption studies of Cu2+ ions.
Zhao et al.  studied melamine-diethylenetriaminepentaacetic acid/polyvinylidene fluoride (MA-DTPA/PVDF)-chelating membranes bearing polyaminecarboxylate groups for removal of Ni2+ ions from wastewater. Salehi et al.  studied adsorption of Ni2+ and Cd2+ ions using 8-hydroxyquinoline ligand-immobilized PVDF membrane.
Na+, Cl−, and SO42− ions are present in significant concentrations in typical seawater and brackish waters . Most of the feeds subjected to desalination processes have sodium chloride (NaCl) or sulfates of Ca and Mg.
Table 3 is a brief literature summary of the electrospun fiber membranes applied to desalination performance. PVDF is generally applied in the as-spun condition. Few data are available on performance of functionalized PVDF for this application.
|Electrospun layer||Second layer/treatment||Solute||Method||Flux (L/m2/h)||Rejection||Ref.|
|PVDF||Polyamides||MgSO4||TFNC by interfacial||0.66||75.7|||
|PVDF||n.a.||6%wt NaCl||AGMD||11–12 kg/m2 h||n.a.|||
|PVDF, clay nanocomposites||n.a.||NaCl||DCMD||n.a.||98.27|
|PET/PS||Polyamides||NaCl||Interfacial||1.13 L m−2h−1bar−1||n.a.|||
|PVDF-HFP (hot pressed)||Hot pressed||NaCl||DCMD||20–22 L h−1 min−2||98|||
|PVDF-PTFE||Microporous PTFE||NaCl||VMD||18.5 kg/m2 h||99.9|||
|PVDF-co-HFP||PAN microfibers||35 g/L NaCl||DCMD||45–30 L h−1 min−2||n.a.|||
|Intrinsically modified PVDF||Ag nanoparticles||3.5 wt% NaCl||DCMD||31.8 L h−1 min−2||n.a.|||
Membrane-based separations and heterogeneous chemical reactions are often treated as independent processes. The advantages of combining the two operations have drawn attention to membrane reactors that combine reaction and separation in a single-unit operation . The properties of PVDF fiber mats naturally lend themselves to use as membrane reactors. The PVDF fiber mats have strength, can be embedded or coated with catalyst particles, have thermal stability over a useful temperature range, are inert to many chemical environments, can be superhydrophobic, and thus provide a barrier to aqueous solutions while being porous to gases.
Catalytic membrane reactors can be fabricated of materials that can selectively remove the reaction products from the reactor to increase the product yield. Membranes as catalyst support structures can provide relatively large surface areas, especially when the electrospun fibers are very small, for supporting catalyst particles .
Inorganic membranes can provide high-temperature durability and easy loading of catalyst . However, polymer membranes have the advantages including flexibility, easy for recycling , and affinity for reagents .
Electrospun fiber membranes have been studied for their physical and chemical properties, mechanical performance , large surface areas, and high porosities . Pinto et al.  studied polystyrene electrospun fibers for catalysts and nanopore filter applications. Electrospun PVDF nanofibers were studied by Li et al.  for immobilizing CoCl2 catalyst for hydrolysis of NaBH4. The high thermal stability, moduli, and mechanical strength of the PVDF fibers showed excellent catalytic activity and recycling stability.
In the work here, palladium (Pd) immobilized on PVDF electrospun fiber mats was investigated for catalytic hydrogenation of phenol to cyclohexanone. The one-step reaction can directly hydrogenate phenol into cyclohexanone, and the hydrogenation can be conducted either in liquid or gas phase. A two-step reaction is also possible in which phenol is first hydrogenated to cyclohexanol and then dehydrogenated to cyclohexanone . PVDF and PVDF-HFP electrospun fiber mats are hydrophobic, resist the flow of water through the membrane, and provide a barrier between phenol water solution and hydrogen gas. Figure 8 has SEM images of PVDF+5% Pd black samples.
Figure 9 shows EDX images of PVDF fibers with Pd black particles. The elemental Pd (appears in green color) on fibers. The fibers appear red due to elemental fluoride. Similar results were obtained for PVDF-HFP electrospun fiber mats.
Batch tests were conducted with Pd supported on PVDF-HFP fibers with 5, 10, and 15 wt% of Pd black. The average fiber diameter was 357 nm. The fiber mats were immersed in 75 mL of phenol/water solution (20 g/L) at 80°C under mild stirring and exposed to H2 gas bubbles.
Reaction sample concentrations were measured by GC. The conversion and selectivity were calculated based on concentration changes. The reaction conversion increased with the concentration of Pd black and reached 98% conversion after 7 hours. The selectivity for cyclohexanone was about 97% for all of the fiber samples.
In this work, PVDF and related copolymer mixtures are discussed. PVDF has unique properties due to its CH2-CF2 repeated monomer units that make it a material of recent scientific interest. Several applications of the electrospun PVDF polymer were reviewed. The PVDF molecule can be polarized. The polarized fiber mats were tested as aerosol filter media. SEM images showed remarkably different performances due to changes in particle capture mechanisms.
The PVDF membranes have potential applications for water treatment, first as a filter but second as a desalination membrane. The inherent dipole charges due to the CH2-CF2 repeated monomer units may be useful for separating salt ions from water. The last topic discussed is the use of PVDF and related copolymers as catalyst supports. As an example, experimental data for hydrogenation of phenol is presented. The limited amount of experimental data available showed that the PVDF membranes can be used for these applications. Further work is needed on these topics to determine the full potential of PVDF and related copolymer electrospun fiber mats.
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