Applications of Polymer Nanofibers. Группа авторов

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Applications of Polymer Nanofibers - Группа авторов

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ρ is solution density, γ is surface tension, η 0 is the zero shear viscosity, Q is the volumetric flow rate, images is the extensional viscosity, ε is the dielectric constant of the fluid, images is the dielectric constant of the surrounding medium (typically atmosphere), and E 0 is the strength of the applied electric field. This analysis explicitly contains the extensional viscosity of the fluid known to control fiber formation. The extensional viscosity can be estimated as 3η 0 for a Newtonian fluid. This approach assumes the final fiber is directly proportional to jet radius in the straight portion of the jet and the actual relationship may be system‐dependent, i.e. influenced by solution conductivity and mechanics of the bending instability (Helgeson et al. 2008). The predictions agree with experimental observations over a broad range of polymer concentrations and voltages. Upon addition of a significant amount of NaCl, the trends are consistent, but the scaling factor changes and may be attributed to the differences in the bending instability.

      Recently, using a force balance on a bent jet considering electric field and surface charge for a Newtonian fluid, Gadkari predicted the final fiber diameter (df) scales as

      (1.8)equation

      where ηo is viscosity, K is conductivity, Q is flow rate, L is tip to collector distance, and V is applied voltage. When compared to experimental results, the scaling prediction qualitatively matches the observed trend for viscosity, flow rate, and applied voltage. The model overpredicts the dependence on volumetric flow rate (0.5 dependence predicted, whereas a 0.3 dependence has been observed experimentally). Experimental values for the scaling relationships for ΔV, L, and K were not available (Gadkari 2014).

      1.2.2 Experimental Results

      Collectively, theoretical considerations indicate that fiber size is affected by applied electric field strength (applied voltage and time to collector distance), volumetric flow rate, and polymer solution (viscosity and conductivity). However, experimental results have been system‐dependent. For example, experiments increasing the voltage has been observed to decrease fiber diameter for many systems such as polyacrylonitrile/DMF and aqueous polyvinyl alcohol due to greater stretching and a stronger electric field. (Andrady 2008). For polyacrylonitrile in DMF, fiber diameter was reduced from ~95 to 50 nm by increasing the voltage from 5 to 25 kV. Conversely, fiber size has increased with increasing voltage. For example, the polystyrene (PS) fibers increased in diameter from 0.31 to 1.72 μm when the applied voltage increased from 5 to 25 kV. The discrepancy in experimental observations indicates that the effect of voltage on fiber size needs to be considered with other process parameters, especially the feed rate and tip‐to‐collector distance. Notably, at higher applied voltages, there is a greater tendency for bead formation. The bead density increased with increasing voltage and the shape of the beads transitioned from spindle‐like to spherical‐like indicating instability of the jet (Ramakrishna 2005).

      Continuous nanofibers of uniform diameter are achieved when the feed rate matches the rate of at which solution is removed from the tip. At lower feed rates, fibers may form intermittently. Higher feed rates increase the tendency to form beads. Given sufficient applied voltage, the average fiber diameter increases with feed rate. Increasing the feed rate can also result in fused fibers. With larger volume of solution drawn from the needle top, the solvent may not completely evaporate. The residual solvent may cause the fibers to fuse together when deposited (Andrady 2008; Ramakrishna 2005).

      Overall, the experimental results generally agree with the scaling analysis, i.e. the final fiber diameter is directly proportional to volumetric flow rate as well as polymer concentration/viscosity. The electric field strength, dictated by the applied voltage and tip to collector distance, also affects fiber diameter. However, various effects have been observed (e.g. increasing the applied voltage may increase, decrease, or have no effect on the fiber diameter depending on the system) due to the complexity of the process. Some authors have performed systematic experiments varying process parameters and used regression analysis (Cui et al. 2007) or neural network models (Sarkar et al. 2009) to establish quantitative relationships. However, these analyses are system‐dependent. There are no methods to date to predict the fiber size based on solution properties and process parameters (Helgeson et al. 2008; Thompson et al. 2007).

      The effect of process parameters (e.g. flow rate, tip‐to‐collector distance, applied voltage) has been widely studied with conflicting experimental results. An alternative approach to tuning nanofiber and membrane properties has been adjusting parameters of the electrospinning setup.

      Generally, electrospinning is performed in air. Controlling the gaseous environment can be advantageous for affecting fiber diameter. To slow the rate of drying, a gas‐jacketed capillary tip can be used to surround the jet with nitrogen saturated with spinning solvent. With slower solvent evaporation, stable Taylor cones could be achieved by electrospinning poly‐L‐lactic acid in dichloromethane (high volatility). Notably, the flow rate of gas affected the rate of electrospinning. Accelerating the rate of evaporation using an external heat source has also been reported to improve the mat quality of hyaluronic acid fibers spun from water. The improved fiber quality was attributed to increased stretching, enhanced solvent evaporation, and a threefold reduction in viscosity due to the flow of hot air (~60 °C). The composition of the gaseous environment is also an important consideration; it affects leakage of the surface charge on the jet to the surrounding environment and ultimately the fiber size. For example, when using Freon‐12 as the electrospinning environment, the fiber diameter was twofold larger than air at the same conditions. This result was attributed to the higher breakdown voltage of Freon‐12 compared to air. With a higher breakdown voltage, the fiber retained

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