Journal of Chemistry

Volume 2014, Article ID 479139, 10 pages

http://dx.doi.org/10.1155/2014/479139

## Two-Dimensional Simulation of Electrospun Nanofibrous Structures: Connection of Experimental and Simulated Results

Department of Chemical Engineering, Faculty of Engineering, Thammasat University, 99 Moo 18, Phaholyothin Road, Klong Nueng, Klong Luang, Pathum Thani 12120, Thailand

Received 23 May 2013; Revised 22 October 2013; Accepted 29 October 2013; Published 20 January 2014

Academic Editor: Davide Vione

Copyright © 2014 Panu Danwanichakul and Duangkamol Danwanichakul. This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

#### Abstract

Nanofibrous mats were obtained from electrospinning Nylon-6 solutions with concentrations of 30 and 35 wt% and were tested for filtration of polystyrene particles in suspension. Some experimental results were compared with the simulated ones. In the simulation, the two-dimensional structures were constructed by randomly depositing a nanofiber, which was assumed as an ellipse with an aspect ratio of 100, one by one. The nanofiber size is assumed to be polydisperse. The results showed that simulated configurations resembled real nanofibers with polydisperse diameters. Fibers from higher solution concentration were larger, resulting in larger pore size, which was confirmed with simulations. Varying the size distribution around the same average value did not make any difference to the surface coverage but it affected 2D pore areas for the systems at low fiber density. In addition, the probability for a particle to pass through the porous structure was less when the fiber density was higher and the particle diameter was larger, which was consistent with the filtration test. Lastly, water flux measurement could yield the void volume fraction as well as the volume-averaged pore diameter, which was found to be greater than the averaged 2D pore diameter from SEM micrographs by the quantity related to the fiber size.

#### 1. Introduction

Electrospinning technique is an easy method to produce nanofibers with size in submicron or nanometer range, by applying the electrical force generated by the electric field between the end of the metal needle and the ground collector. The liquid source for spinning fibers may be a polymer melt or a polymer solution. A polymer melt or a polymer solution is placed in a syringe. Once the applied electrical force is greater than the surface tension of the hanging hemisphere drop at the end of the syringe needle, the liquid is pulled out of the needle and swirled onto the collector surface. Continuous fibers are produced in this manner. While the solvent evaporates, the final nonwoven nanofibrous structure is solidified. A large number of papers discussing the production of nanofibers from various polymer systems and their applications have been published [1–5]. The research on nanofibers is still receiving more and more attention. Indeed, the benefit of large surface area to volume ratio of nanofibrous structures improves their performance in many aspects including higher mechanical strength, an increase in surface activity, and an increase in adsorption capacity. Therefore, nanofibers were widely studied for use as sensors [1], catalysts [2], drug delivery systems [3], tissue scaffolds [4], and filters [5]. The study about surface characterization and pore generation of nanofibrous membranes is, thus, of great interest.

There are many factors influencing the size of fibers produced via electrospinning. Those are voltage of power supply, distance between the needle tip and the ground collector, solution flow rate, viscosity, conductivity, and surface tension of polymer solutions. Some of these process parameters were modeled by Danwanichakul et al. by using poly(vinyl alcohol) as a model polymer [6]. However, not only fibers but also the pores generated by the overlap of fibers themselves are of importance. H.-S. Park and Y. O. Park found that pore size distribution in nanofibrous structures was narrow or sometimes monodisperse [7]. The experiment was performed but there was no explanation for that. The theoretical work could then fill the gap. Eichhhorn and Sampson simulated the fibers by assuming that they are of cylindrical shape whose diameter is much smaller than the length [8]. They found that if the mass of fibers per unit area was fixed, when the mass of the fibers increased, the average pore size increased. Maze et al. simulated the filter using nanofibers with a diameter of 200 nm and allowed the particles with diameters between 50 and 500 nm to pass through the pores. They found that the pressure drop was related to the pore size as could be predicted by fluid mechanics [9]. In addition to 2D simulations, Hosseini and Tafreshi attempted to simulate 3D nanofibrous structures by building rigid cylindrical fibers one by one on top of each other and used computational fluid dynamics to study the collection of particles in the air when passing through these simulated filters [10]. Another attempt to create 3D nanofibrous structure was made by Sambaer et al. in the simulation of filtration process via polyurethane nanofibers [11]. To construct fiber mats, an image of top layer of fibers was used as a template for creating the whole mats with multiple layers. This method was proved successful in imitating the real behavior of the nanofibers in filtration process.

The success of 3D-simulation by Sambaer et al. [11] was, however, based on the 2D structures of the nanofiber network so the knowledge of 2D structures is still important. All papers about simulation of electrospun nanofibers involved the filtration of aerosol and assumed that the fiber size was monodisperse. In this work, nylon-6 was selected as a model polymer and smooth nanofibers produced by electrospinning were applied in filtration of particles from liquid suspension. The 2D simulation was performed to study the effect of fiber size polydispersity on the pore size of the nanostructures as well as to connect the simulated results with the experimental results either qualitatively or quantitatively.

#### 2. Material and Method

##### 2.1. Materials

Nylon-6 was purchased from Sigma-Aldrich Co. LLC. Formic acid was supplied by Ajax Finechem Pty Ltd. The suspensions of polystyrene particles with average particle sizes of 90 nm (50–100 nm) and 200 nm (200–300 nm) were purchased from Spherotech, Inc. All chemicals were of analytical grade and used without further purification.

##### 2.2. Electrospinning of Nylon-6 Nanofibers

Nylon-6 was dissolved in 10 mL of 90 wt% formic acid to obtain the spinning solutions with concentrations of 30 and 35 wt%/vol, namely, N6-30 and N6-35, respectively. Each mixture was blended with a magnetic stirrer at room temperature for 2–4 h until the solution was homogeneous. The spinning solution was poured into a 2 mL syringe with a needle whose inner diameter and length were 0.514 mm and 4.2 cm, respectively. A high voltage power supply (Glassman PS/MJ30PO400) was connected to the needle end by a stainless steel electrode. Another electrode was connected to the stationary collector covered with 3.5 × 3.5 cm^{2} copper plate. The voltage was set at 21 kV and the distance between the needle tip and the collector was held constant at 9 cm. The spinning time was about 1.5–3 h in order to obtain the 0.1 ± 0.02 mm thick nanofiber mats. The spinning was performed without a syringe pump so the polymer solution was purely pulled out of the needle tip by electrical forces. However, the flow rates could be measured to be 3.33 and 1.94 *μ*L/min for N6-30 and N6-35 solutions, respectively, reflecting the effect of solution viscosity.

##### 2.3. Morphology of Nanofibers

The morphology of nanofibers was observed with scanning electron microscope (SEM) (JEOL JSM-6310F) after coating by a gold sputtering coater for 100 seconds. Each SEM figure was analyzed for the average fiber size as well as the apparent average pore size of the structure. The fiber diameter and pore size were measured by comparing with the scale bar on the SEM figures. The average was from at least 100 samples. The fiber diameter was measured along the axis perpendicular to the fiber length and the pore size was measured along the horizontal axis by adopting the widest distance as the pore size. The 2D pore area could be determined rigorously by filling up the pore with small circular discs whose areas were known. The number of the discs reflects the area of the pore. To obtain the fiber coverage on the surface, the grey scale analysis was performed with the simulated figures. Fibers and vacant areas can be differentiated by the color so the fraction of deposited area could be determined.

##### 2.4. Water Flux Measurement

In this experiment, a syringe containing 5 mL water was vertically connected to a filter holder inside which the filter medium was placed. A 0.5 kg piece of metal was then placed at the end of the syringe, pushing the water to pass through the circular filter medium whose diameter is 13 mm. The flow is so slow that it could be considered a laminar flow and the volumetric flow rate of water could be measured. Pores inside the nanofibrous structure are usually interconnected so the structure resembles a bundle of tortuous tubes. The volume-averaged pore size could be determined using the relationship between water flux and pressure drop across the membrane as the expression in the following: In (1), is the superficial velocity (m/s), is the viscosity of water at 30°C , is the filter thickness (m), is pressure drop (Pa), is the void fraction, is the tortuosity, and is the volume-averaged pore diameter (m).

##### 2.5. Filtration of Polystyrene Particles

Firstly, the nanofiber filter was placed in the filter holder with a diameter of 13 mm and 5 mL of 200 ppm polystyrene particle suspension was pumped through the filter by a syringe pump at a fixed flow rate of 8 *μ*L/sec. The polystyrene (PS) colloidal particles were collected by the filter and the concentration of the filtrate was measured by using the calibration curve showing the linear relationship between the concentration and absorbance measured with UV-VIS spectrophotometer at 490 nm. The filtration efficiency is expressed as
Here, and are the initial concentration of PS particles in suspension and the concentration in the filtrate coming out of the filter, respectively.

##### 2.6. Computer Simulation of Nanofibrous Structures

The computer program was written in FORTRAN in this study. The deposition of fibers on a surface was performed by Monte Carlo simulations. First, the position on the 2D system and the size of fibers are randomly sampled one by one. Each “2D” fiber is modeled as an ellipse whose aspect ratio, that is, the ratio of the long axis length to the short axis length, equals to 100. The length of short axis of the reference fiber is set at which is scaled with a unit size as . The deposited area is scaled as , equivalent to the area of the surface whose width and length are equally . Therefore, the fiber size is 150 nm and the deposited square area is 5 × 5 *μ*m^{2} when the size is set as 500 nm. Not only the position of the fiber center but also the angle of the fiber major axis with respect to the -axis is sampled randomly on the surface.

To study the effect of fiber size, the size polydispersity of the fibers was varied according to the uniform size distribution to be , , , and , where is the size of reference fiber which is as described above. The simulated structures were analyzed for the surface coverage on the deposited area and the average pore size of the structures when more fibers were deposited.

To quantify how difficult the particles will pass through the 2D porous structures as in the filtration test, the number of attempts for the particle to deposit on the structure was measured until it could successfully pass the 2D pore. The number of attempts reflects the probability of capturing the particles inside the nanostructures. In this test, the particle diameter was varied as , , and and the fiber diameter was fixed at .

#### 3. Results and Discussion

##### 3.1. Morphology of Nanofibers

SEM micrographs of electrospun products from solutions of different nylon-6 concentrations are shown in Figure 1. The left-handed side represents the structures from 30 wt% nylon solution while the right-handed side was from 35 wt% solution. The image analysis of SEM figures yielded the average diameters of fibers and pores of the structures, which are also shown in the figure. Upon increasing the concentration from 30 wt% to 35 wt%, the average diameter was increased from 103 to 144 nm because of an increase in solution viscosity [12]. It is clearly seen from the SEM figure and the size distributions of both fibers and pores that the larger fibers could form the structures with larger pores [13]. The average pore size was estimated to be 94 nm and 154 nm for N6-30 and N6-35, respectively.

##### 3.2. The Simulated 2D Nanostructures

The number of deposited fibers on a unit area is defined as the number density of fibers. For instance, the system with number density of 0.1 contains 10 fibers on area. The structures are shown in Figure 2 where the number density increases from 0.1 to 0.8 for the structures composed of the same fiber size of . However, since the actual structure contains fibers with polydisperse size as shown in Figure 1, the simulation was then done to obtain structures of various size distributions as displayed in Figure 3.

In Figure 3, all samples are compared at the same fiber number density of 0.8. It could be seen that the fiber size could be differentiated from one another more easily as the size distribution is wider and this realization is similar to what is seen in the SEM figures. The information that could be obtained from the simulated figures using the gray scale analysis is the surface coverage of the nanofibers at different number densities. The knowledge of surface coverage is important in the applications of surface coating with nanofibers in order to modify the hydrophilicity or hydrophobicity of the original surfaces by using more hydrophilic or more hydrophobic nanofibers. For instance, the superhydrophobicity of the surface confirmed with water contact angle measurement was reported when coating fluorine-plasma-treated cellulose nanofibers on microfiber, which possessed large surface areas [14]. Another example dealing with surface coverage is that the minimum amount of nanofibers was also deposited on top of the large fiber filter to increase the filtration efficiency [15].

##### 3.3. The Closeness of Simulated Structures and the Real Nanofibers

In order to compare the 2D nanofibrous structures with the simulated ones, the system of N6-35 was chosen. The average fiber size is 144 nm while the simulated average fiber size, , is 150 nm on 5 × 5 micron^{2}. As seen in Figure 1, the size distribution of the fibers ranges from 70 nm to 225 nm so the closest distribution for the simulated fibers chosen for comparison is , which corresponds to 82.5 nm to 217.5 nm. The simulated structure and its pore size distribution are displayed in Figure 4. It is seen that when the fiber number density is 0.3, the pore size distributions of simulated and SEM figures (Figure 1) are consistent. The pore size from SEM figure could be as large as 670 nm. The average pore size of simulated structure is 165 nm which is close to 154 nm of the SEM figures. Therefore, it is possible to simulate the electrospun nanofibers in 2D to make them resemble the real structure.

The comparison could also be made by fixing the solid volume fraction (SVF) or solidity of the structures with different fiber size distribution. The solid volume fraction ranges from very low to 13% [10]. The comparison of simulated structures is shown in Figure 5. The figure shows the structure of simulated nanofibers of the average size around 100 nm, which corresponds to N6-30, and that with average size around 150 nm, which corresponds to N6-35, at the same solid volume fraction. If the thickness of the membrane is assumed to be the same, the number density is then inversely proportional to the squared fiber diameter. Therefore, to be compared, the number densities of the two systems are 0.45 and 0.2, respectively. It is evident that at the same solid volume fraction, the pore size of the structures containing large fibers is larger as previously seen in Figure 1.

##### 3.4. The Surface Coverage of Nanofibers and Projected Pore Area

The surface coverage and the average pore size of the corresponding simulated structures in Figure 3 are illustrated in Figures 6 and 7, respectively. The size of the fibers was varied according to a uniform distribution, where the lower limit and upper limit need to be specified. The sampled fiber size within this range will have the same probability. The chosen lower limits and upper limits of the fiber sizes are , , , and . It should be noted that all uniform distributions applied in this work are around the same average fiber size of , the value at the center of the two limits. Accordingly, the width of size distribution was wider as could be seen from the difference between the lower and upper limits which is , , , and , respectively.

The gray scale analysis with Photoshop was applied in this study. Differentiation between the deposited area (gray area) and the available area or porous area (white area) could be done by the program. These monotonous results show that all samples had the same coverage area even though the fiber sizes could be differentiated. This happens probably because the chosen size distribution is still too close to each other and all distributions have the same average size which is . This may be considered as a confirmation that if the *average size* of nanofibers could be controlled to be equal for all samples, the surface coverage of the fibers could be pretty much the same, independent on the fiber size distribution in the ranges studied here.

The effect of number density on the surface coverage is clearly seen in Figure 6. The coverage certainly increases upon increasing the number density but the increase rate is slower at higher density due to higher chance of fiber overlaps as seen in two dimensions. However, upon adding more fibers, the projected pore sizes of the structures decrease as shown in Figure 7. In the figure, it is obvious that an increase in fiber density could decrease the pore size of nanostructures rapidly at low fiber density. The pore size decrease rate is lower when the fiber density increases due to less probability for fibers to deposit on the vacant area. The transition is seen at density of 0.2 or it may be thought as a crossover of the pore generation mechanism. At a high fiber density on the surface, it could be seen that there are lots of small pores the size of which is around 1-2 times the fiber size. Figure 7 also shows similar results of the average pore areas when the size distribution was varied. The discussion was already given earlier. However, the difference was clearly seen at the low coverage of the fiber. It seems that for a low fiber density, the distribution that contains the larger size range results in smaller pore area. The 2D structure at a low density is important in simulation of nanofibers in 3 dimensions where the whole membrane is made of layers of thin 2D networks [11].

##### 3.5. The Probability of a Particle Passing through 2D Pores

Since one of the applications of nanofibers is being used as a filter, with these simulated structures, it is possible to obtain the probability for a particle to successfully move through the pores perpendicular to the direction of the flow. In this test, particles are sampled one by one to be deposited in the pore as described by ballistic deposition model. The number of attempts made to successfully place the particle in the pore, that is, the particle does not overlap with the fibers, is counted. Therefore, the reciprocal of this number is the probability of the particle passing through the filter without being intercepted by the fibers. The results are shown in Figure 8, where the size of the particles is varied while the size of the fibers is fixed at .

It is found that at the same fiber number density, larger particles tend to stick more easily to the fibers than the smaller particles, yielding higher efficiency of the filtration [16]. However, in a real situation small particles could aggregate because of their high surface energy which results in large agglomerates leading to a high efficiency in filtration. It was reported that there is an optimum size range for particles to easily get through the filter [9]. Particles smaller than this size range could form an aggregate which is larger than the pore size and particles larger than this size range are larger than the pore size. The topic of aggregation will be investigated more in the future. The number density in this case actually correlates with the thickness of the filter in 3D. As the number of fiber increases, the thickness of the membrane increases and this certainly increases the filtration efficiency with an expense of high pressure drop across the membrane [15].

The experimental study of filtration of small particles with nylon-6 nanofibers was also done in this work. With a membrane the thickness of which is around 0.1 mm, the N6-30 samples could completely remove all particles from the 200 ppm polystyrene particle suspension; that is, the separation efficiency according to (2) equals 100%. Figure 9 shows the filter fronts where particles with diameters of 90 nm and 200 nm were captured. The outline of the nanofibers are still seen for the case of smaller particles while almost complete surface coverage is seen for the larger ones, implying higher probability for smaller particles to move inside the pores of nanofibrous structures as was seen in the simulations.

##### 3.6. The Void Volume Fraction and Tortuosity of the Structures

Based on the Kozeny-Carman relation, which could well describe the pressure drop of laminar flow through fibrous mats, the void volume fraction of the nanostructures could be estimated [17]. The equation was modified here to take into account the tortuosity of the structures and the actual velocity of the flow: In (3), is the superficial velocity (m/s), is the viscosity of water at 30°C (), is the filter thickness (m), is pressure drop (Pa), is the void fraction, and is the tortuosity; is the Kozeny constant, which is equal to 0.55 for nearly cylindrical fibers if void fraction () varies from 0.6 to 0.8.

The tortuosity could be approximated by realization that the whole fibrous mat is composed of many layers of nanofiber networks. Each layer is very thin and the surface coverage is equal to *. *Thus, the probability of liquid to pass through each layer is , which is equivalent to void fraction, . The thin layer of thickness is considered and the liquid is divided into parts. If some parts of the liquid could pass directly through this layer then the traveling distance of these parts is . The other parts are blocked by the fibers so the liquid has to move laterally for a distance , in case the available pore is located at the distance from the fiber. Still there are liquid parts that are blocked by the fibers and have to travel farther with a distance . It is obvious that the probability for the liquid to find the pore depends on the void volume fraction. With this logic, one could write the equation of tortuosity which is defined as the ratio of actual distance for the liquid to travel to the mat thickness. The actual distance is the average of traveling distance of all liquid parts. Therefore, we have
The number of terms in (4) could reach infinity so tortuosity could be approximated as

The fixed volume of water was fixed at m^{3} and the weight pushing the water through the filter was also fixed at 6.42 N. The filtration time was recorded as shown in Table 1 and the void fractions of N6-30 and N6-35 mats can be calculated.

It is noted that as seen from the SEM images in Figure 1 and simulated images in Figure 5, the pore size is larger when the deposited fibers are larger and this could affect the void fraction as a whole so N6-35 had higher void fraction than N6-30. Based on this value, one could assume the first layer is the network with surface coverage equal to , which is 0.252 and 0.281 for N6-30 and N6-35, respectively. According to Figure 6, for N6-35 with the surface coverage about 0.3, the number density is a bit larger than 0.1. If the structure with density of 0.1 is adopted for the first layer, the multiple layers could be built layer by layer to obtain the whole mat as previously done by Sambaer et al. [11]. Thus, using the connection of the experimental results and simulated results, one could have a guide to construct the structure of each layer.

##### 3.7. The Average Pore Size Determination

Based on the water flux measurement as discussed in the previous section, the Hagen-Poiseuille equation, (1), could be used to estimate the volume-averaged pore size [18]. The equation was derived for the flow in circular pipe so, in this work, the channel inside the structure is assumed to be little tortuous circular pipes with nonuniform cross-sectional area. The volume-averaged pore size was obtained as shown in Table 2.

From Table 2, it is found that the volume-averaged pore size obtained from Hagen-Poiseille equation is larger than the pore size obtained from SEM figures. If the volume-averaged pore size is considered as 3D pore size, , and the average from SEM image as 2D pore size, , it is possible to relate two quantities by Equation (6) was used to estimate for N6-30 and N6-35 and it is found that ’s are 139 nm and 210 nm, respectively, being compared with 181 and 216 nm. The numbers imply that in three dimensions, the pores are generated by the deposition of one fiber on top of other fibers so the space along the axis of membrane thickness between two fibers is at least equal to the fiber diameter as was assumed when 3D simulated structures were created by Hosseini and Tafreshi [10]. This is seen in our example of 3D structure of N6-35 shown in Figure 10. The structures were built by adding one fiber at a time on top of the previously added fiber.

#### 4. Conclusions

The simulation of nanofibrous structures via Monte Carlo method in 2 dimensions was performed. The results confirmed that even though there are some variations in fiber size, if the average size of fiber could be controlled, the surface coverage of fibers randomly deposited during electrospinning process could be the same. However, at a low number density of fiber, the average pore size was different when the fiber size range was varied. This structure may be considered as a structure of initial layers that could be used to simulate the 3D structures by combining multiple thin 2D networks together as a whole mat.

The simulated structures resembled real SEM images of nanofibers closely since the fiber size distribution and the average size of the fibers were chosen to be close to the real systems, confirming efficiency of 2D simulations. Calculations of void fraction and tortuosity of the structures could be used to prove that the space between two fibers along the axis of membrane thickness is at least equal to the size of the fibers deposited, providing the connection between 3D pore size and 2D pore size from the SEM figures or from the simulated 2D figures.

#### Conflict of Interests

The authors do not have any conflict of interests regarding this research work.

#### Acknowledgments

This research was jointly funded by the Thailand Research Fund (TRF) and Thammasat University (Grant no. DBG5380007). All assistance from the Faculty of Engineering is highly appreciated.

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