Aqueous solution blow spinning of poly(vinyl alcohol) micro- and nanofibers Adillys M. C. Santos a, Eudes L. G. Medeirosa, Jonny J. Blakerb, Eliton S. Medeirosa* a Materials and Biosystems Laboratory (LAMAB), Department of Materials Engineering (DEMat), Federal University of Paraiba (UFPB), CEP58051-900, João Pessoa- PB, Brazil. b Bio-/Active Materials Group, School of Materials, MSS Tower, Manchester University, Manchester, M13 9PL, UK E-mail: [email protected] Abstract This work addresses the challenge to produce fibers from the water-soluble polymer poly(vinyl alcohol) (PVA), using solution blow spinning (SBS) with forced solvent evaporation at the point of fiber formation. PVA at two different molecular weights, with different degrees of acetylation, were successfully blow spun into nanoand micro-fiber membranes, across a range of concentrations in water (12-20 w/v%). Fiber spinnability, morphology and size are correlated to precursor solution viscosity and PVA type. PVA with degree of polymerisation 1100 and degree of hydrolysis 9899% was relatively facile to spin into fibers. Difficulties in spinning high molecular weight PVA were overcome by introducing hot air at the point of fiber formation to force water evaporation. The procedure developed here opens SBS to other aqueousbased polymer and composite systems for environmentally benign fiber and membrane formation. Graphical abstract Keywords: Solution blow spinning, poly(vinyl alcohol), nanofibers membranes 1. Introduction Solution Blow Spinning (SBS) is a simple rapid technique to produce nanofibers, using pressurized air-stream as driving force for fiber formation. SBS overcomes some drawbacks associated with electrospinning such as the use of electric field. The high velocity airflow used in SBS aids solvent evaporation for dry fiber production [1]. Most published work on solution blow spinning involves the use of highly volatile organic solvents (or solvent mixtures)[2,3]. Spinning from low volatile solvents like water is challenging since the fibers do not fully dry before reaching the collector, causing the fibrillar morphology to be destroyed by coiling of polymer molecules. Poly (vinyl alcohol), is a water soluble and semi-crystalline polymer obtained from controlled hydrolysis of poly(vinyl acetate) (PVAc). PVA has good chemical and thermal stability, is nontoxic and biocompatible with a wide spectrum of applications[4,5]. Electrospun fibers from PVA have been studied with respect to production parameters including molecular weight [6,7], concentration [7–9], and with nanofillers, including cellulose nanocrystals [10], carbon nanotubes [11] , silica [12], and hydroxyapatite [13]. PVA biofibers have been processed by SBS [14]. Here, PVA aqueous solutions are spun into fibers applying a modified SBS heads and forced evaporation using heat applied at the air exit. Fiber spinnability, morphology and size are correlated to precursor solution viscosity and PVA type. 2. Experimental 2.1 Preparation and characterization of the polymer solutions PVA-110 (degree of polymerization 1100 (Mw 49,000 g.mol-1); degree of hydrolysis 98-99%) and PVA-224 (Mw 118,000 g.mol-1; degree of hydrolysis 87-89%) were kindly donated from Kuraray Ltd, Brazil, in powder form. These dissimilar physicochemical properties were chosen to study their influence on the solvent evaporation. PVA was dissolved in distilled water at 12, 16 and 20 w/v%, under constant stirring, at 90 °C for 2h. Rheological properties were assessed using a coneand-plate rheometer (AR2000, TA instruments, USA), disc diameter of 40 mm, by varying the angular frequency from 1 to 100 rad.s-1and applying the Cox-Merz rule [15]. 2.2 Fiber spinning methodology and characterization The SBS apparatus and detail of the concentric nozzles is shown in Figure 1. Aqueous PVA solutions were injected into the inner nozzle at 120 µL.min-1, with the outer nozzle supplying pressurized air at 0.55 MPa. The inner nozzle tip (diameter 0.7 mm) protruded the outer one by 15 mm. When necessary, a Bunsen-burner with the air vent and gas flux adjusted to get the coolest output flame, which was suitable yelloworange in color, was positioned below the SBS nozzle (see Figure 1). This acted to increase the temperature of the air exiting the annulus at high speed, which draws the heat to the point of fiber formation. Interestingly, the temperature at the vicinity of air exit was measured at 30°C and at the point of fiber formation about 45 °C, both assessed with a digital thermocouple, and arrowed in Figure 1. The morphology of the resultant fibers were assessed on gold sputter coated samples using scanning electron microscopy (SEM, FEI Quanta 450, Czech Republic, at 8 kV). Fiber diameters were measured using ImageJ (Version 1.48, NIH, USA), with 50 individual fiber measurements per sample at two different sites. 3 Results and discussion 3.1 Rheological measurements The viscosity of the solutions increased with increasing concentrations, with the PVA-224 exhibiting higher viscosities than PVA-110 across all concentrations (Figure 2a), consistent with previous literature [7]. Newtonian behavior was observed at all shear rates, with the exception of the 20 w/v % concentration, which exhibited some o shear thinning behavior. The apparent shear rate app in the inner nozzle channel was estimated assuming classical Newtonian flow for the 7 mm long nozzle portion, as indicated in Figure 1. The well-known rheological relation for the capillary tube o app 4Q / r 3 was used, where Q is the volumetric flow rate and r is the capillary diameter [15] and the apparent shear rate found was 60 s-1. At this shear rate, it was possible to assess the apparent viscosities of the solutions (Figure 2b), and ultimately evaluate their effect on the fiber diameter, discussed below. 3.2 Fiber spinnability and morphological characterization Fiber formation was relatively facile for the low molecular weight PVA-110, using the protruded nozzle set up. At a low concentration (12 %w/v), unstable jets of fibers and droplets formed, resulting in bead-on-string structures (Figure 3a). While some of these fibers were individualized and loose, many were conjoined due to incomplete water evaporation, consistent with previous observations of electrospun fibers [16]. The fibers presented a circular cross-section with a mean diameter of circa 302 ± 99 nm. Increasing PVA concentration to 16 and 20 w/v% resulted in smooth and larger diameter fibers (450 ± 155 nm, and 1040 ± 440 nm, respectively), Figure 3b-c. Increasing the polymer concentration in solution enhances chain entanglement, causing the jet to resist deformation [10], resulting in thicker fibers (Figure 2b). PVA-224 solutions presented difficulties in the spinning process employing the setup used for PVA-110. Irrespective of the solution concentration, little fiber formation was observed, probably due to insufficient water evaporation. Instead of fibers being predominant, a wet, film-like membrane with few discernible fibers was observed (see supplementary information). The mean diameters of these few fibers were 655 ± 380 nm, 1240 ± 290 nm and 1920 ± 1320 nm, for polymer concentrations at 12, 16 and 20 %w/v, respectively (Figure 2b). With the aid of the heat source, interestingly, the flame tip was pulled towards the annulus tip due to the SBS gas stream (see graphical abstract) and the fibers instantaneously appeared in the airstream. The heat was enough to guarantee a balance between deformation and water evaporation. The morphology of fibers at 12 w/v% and 16 w/v% were relatively smooth, with mean diameters 571 ± 232 nm, and 1551 ± 395 nm, respectively (Figure 3d-e). It was not possible to spin PVA-224 at 20% w/v concentration due to clogging at the inner nozzle. Heating the entire concentric nozzles setup may lead to polymer degradation and poor final fiber properties. Here, the protruding setup was more suitable for the spinning process and avoided the flame tip to hit the polymer solution directly and, accordingly, the clogging effect. In aqueous solutions there is inter- and intra-chain bonding between the PVA chains and the water molecules after dissolution [17], which can reform during solvent evaporation. At a constant solution concentration, increased PVA molecular weight and hydrolysis degree act to increase viscosity, reducing solvent evaporation. In contrast, the rate of solvent evaporation is relatively high at a low molecular weight and the fibers essentially dry before reaching the collector. Even though water evaporation is enhanced with decreasing degree of hydrolysis, the high degree of polymerization of PVA-224 increases the viscosity and reduces water diffusion and evaporation. Accordingly, a heat source was required to achieve high yields of fiber formation and reduced diameters. Conclusions Micro- and nanofibers were successfully solution blow spun from aqueous solutions of PVA. Mean fiber diameter was found to be dependent on the solution concentration and molecular weight. Low molecular weight PVA (Mw 49,000 g.mol-1) was relatively facile to spin into fibers using a protruding inner nozzle, with a relatively high-pressure air (pressure supplied at 0.55 MPa). Fiber formation from aqueous solutions of higher molecular weight PVA at 12 and 16 w/v% concentrations was aided by a heat source (Bunsen burner), heat of which was drawn into the point of fiber formation, acting to locally heat the air to 45°C. Concentrations of high molecular weight PVA at 20 w/v% were not spinnable due to clogging, whereas the lower molecular weight could be spun at 12, 16 and 20 w/v%. This work opens the SBS technique to other water-soluble polymers and composite systems for environmentally benign fiber and membrane formation. Acknowledgements AMCS, JJB and ESM acknowledges support from CNPq (Brazil), grant number 400248/2014-0 and to Professor Sandro Torres and Meyson Nascimento for the assistance with SEM. References [1] E. S. Medeiros, G. M. Glenn, A. P. Klamczynski, W. J. Orts, L.H.C. Mattoso, Solution blow spinning: a new method to produce micro- and nanofibers from polymer solutions, J. Appl. Polym. Sci. 113 (2009) 2322–2330. [2] R.E. Benavides, S.C. 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Levinskas, The influence of main technological parameters on the diameter of poly(vinyl alcohol) (PVA) nanofibre and morphology of manufactured mat, Mater. Sci. 13 (2007) 3–6. [17] P.D. Hong, C.M. Chou, C.H. He, Solvent effects on aggregation behavior of polyvinyl alcohol solutions, Polymer (Guildf). 42 (2001) 6105–6112. Figures Figure 1. (a) Schematic of the SBS set-up for forced aqueous solvent evaporation, indicating the position of the heat source used, and (b) positions of the temperature assessed (arrowed), and nozzle detail. Figure 2. (a) Viscosity values and (b) their influence on fiber mean diameter. Figure 3. SEM micrographs of solution blown spun fibers of PVA-110 at different polymer concentration (without heat applied, a-c), and for PVA-224 temperatureassisted (d, e). Supplementary Information: Figures Figure S. SEM micrographs of solution blown spun fibers of PVA-224 at different polymer concentration (without heat applied, a-c).
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