Abstract
Enrichment of chemically resistant hydrophobic polymers with polar biomolecules is relevant to the production of fiber-based drug delivery devices and adsorptive filtration media, as well as fibers for selective molecular recognition of antibodies, enzymes and nucleic acids. Polysulfone (PSU) is an amorphous polymer possessing high-strength, rigidity and excellent thermal stability. The preparation of PSU spinning solutions requires lengthy dissolution times at elevated temperature that tends to degrade commixed polar biomolecules. Using the highly polar metabolite creatinine, as a model system, a variety of co-solvents was evaluated for electrospinning commixed solutions of PSU and creatinine at room temperature. The selection of solvent systems was informed by Hansen solubility parameters. A binary system of N, N-dimethylacetamide (DMAc):methanol (4:1) was not found to be a suitable solvent because of the need for elevated temperature (80℃) to facilitate dissolution, and a binary solvent system of N, N-dimethylformamide (DMF):dimethyl sulfoxide (DMSO) (3:2) resulted in nozzle blockage during spinning. A binary system of DMAc:DMSO (13:7) enabled preparation of PSU with creatinine at ambient temperature, and sub-micron fibers substantially free of beads were produced continuously via electrospinning, yielding fiber diameters in the range 470–870 nm. The presence of creatinine was confirmed by high performance liquid chromatography (HPLC), and fiber morphology was examined by scanning electron microscopy (SEM).
Sub-micron fibers of high specific surface area with properties enhanced by chemical enrichment of chemically resistant polymers are important for the development of devices for use in regenerative medicine, adsorptive apheresis, blood filtration, as well as in the delivery and release of drugs and biological agents such as proteins.1–4 For example, in the preparation of alternative molecular recognition membranes, a template molecule is incorporated in the spinning solution, which is later eluted after fiber or membrane production to provide chiral recognition sites. To facilitate production, a co-solvent system is often needed in which both the polymer and biomolecule components can be dissolved. The resultant templated fibers are potentially useful as sorbents or sensors provided rigid, hydrophobic polymers are selected to ensure structural stability of the template cavity.5,6 Similarly in the preparation of drug delivery systems, the ability to commix both the fiber forming polymer and the drug in a co-solvent without degradation of the therapeutic compound prior to manufacture is important.
Many hydrophobic, thermoplastic polymers used in medical devices particularly polysulfone (PSU), polyphenylene sulfide (PPS), liquid crystal polymers (LCP), polyethylenimine (PEI), polyamide-imide (PAI) and poly(aryl-ether-ether-ketone) (PEEK) have high chemical resistance to solvents, which means spinning solutions containing such polymers are likely to be incompatible with water soluble biomolecules. Chemical resistant polymers with a rigid and highly cross-linked network structure often require lengthy dissolution times at elevated temperature that are likely to degrade biomolecules that need to be present in the solvent. 7 The incorporation of biomolecules into such polymers without chemical degradation can therefore be highly challenging.
Accordingly, the aim was to identify suitable co-solvents for the spinning of PSU using a model, highly polar, water-soluble biomolecule, creatinine (C4H7N3O), at room temperature. Creatinine, one of many uremic toxins, is the metabolic product of phosphocreatine produced by muscular activity and is a cyclic derivative of creatine that is soluble in both water and methanol. 8
PSU is an amorphous polymer that possesses high-strength, rigidity and excellent thermal stability, maintaining these properties over a wide temperature range.9–11 Previous studies have highlighted the chemical stability of PSU and its poor solubility in supercritical fluids (SCF), butane, dimethyl ether (DME), chlorodifluoromethane and difluoroethane, even at temperatures as high as 200℃ and pressures of 2100 bar. 12 Solubility was observed in DME with the addition of 24–65 wt% tetrahydrofuran (THF) or N,N-dimethylformamide (DMF), at room temperature/pressure 12 but such a solvent system is likely to denature biomolecules present in a commixture.
The dissolution of PSU requires solutions to be stirred at elevated temperatures, between 45–120℃.7,8,13 Wang et al. 7 dissolved PSU powder in N, N-dimethylacetamide (DMAc) at 120℃ with vigorous stirring to form a homogenous solution with poly(N-vinyl-2-pyrrolidone) (PVP). Li et al. 8 dissolved 25 g PSU pellets in 90 ml DMAc and 10 ml acetone with stirring for 4 hr at 45℃. 8 Previous studies producing PSU electrospun webs have frequently used DMF and DMAc as the solvent system;7,13,14 however, the dissolution of creatinine is impossible in the solvents that are normally used to dissolve PSU to make an electrospinning solution.
Creatinine is a polar molecule and is known to be soluble in both water and methanol but sparsely soluble in acetone. Thus, one cornerstone of this work was to identify an appropriate co-solvent system for PSU and creatinine that would enable the dissolution of both components at near ambient temperature to avoid creatinine degradation and to facilitate electrospinning.
Material and methods
Materials
PSU pellets (Mw: 35,000) were purchased from Aldrich Chemical Co., and creatinine (99%) was obtained from Acros Organics Co. DMSO, DMF, methanol, acetone, DMAc and ethanol were all purchased from Sigma-Aldrich Co. and used without further purification. Di-sodium hydrogen phosphate and citric acid were purchased from Fluka Co.
Preparation of the PSU solution
The solubility of polysulfone (PSU) in different solvent systems
DMAc: N, N-dimethylacetamide; DMF: N, N-dimethylformamide; DMSO: dimethyl sulfoxide.
Electrospinning
Electrospinning was performed in horizontal alignment with the polymer solution loaded into a 5 ml syringe (Fortuna and Graff) connected to a blunt-ended Luer lock metal needle (20 gauge, Sigma-Aldrich). The syringe was mounted into a syringe pump (KD Scientific) connected to a high voltage power supply (Glassman Inc.). Electrospinning was performed inside a fume cupboard under ambient conditions at a fixed voltage of 25 kV and a tip–collector distance of 130 mm. The spinning solution feed rate was varied between 0.004–0.02 ml min−1. Flat aluminum foil collectors were used throughout.
Scanning electron microscopy and image analysis
Samples were sputter coated then imaged using field emission scanning electron microscopy (SEM) (Camscan series 4 environmental) to observe the fiber morphology and web structure. Mean fiber diameters in the collected webs were determined directly from the SEM images by image analysis (Media Cybernetics, Image Pro-Plus 7) by measuring the diameter of 50 individual fibers. To estimate the porosity (P) of the webs, binary SEM images (bitmap format) were prepared by image thresholding techniques and determined from the mean intensity of the image as follows
Pore size
Pore size characterization of the as-spun webs was undertaken by capillary flow porometry (PMI model App122 AE). All pore structure characteristics including pore size at the bubble point and pore size distribution were computed from the measured differential pressures and gas flow rates. In the dry sample, the flow rate increases with pressure. In the case of wet samples that are pre-saturated with a liquid of known surface tension (Galwick liquid: surface tension = 0.015 Nm−1), there is initially no flow because all the pores are filled with the liquid. At a certain pressure, the injection of nitrogen gas empties the largest pore (bubble point) and gas flow commences through the wet sample. Further increases in pressure progressively empty the smaller pores and the flow rate increases until all the pores are empty and the flow rate through the wet sample is the same as that through the dry sample.
Molecular analysis
The presence of creatinine was verified by high performance liquid chromatography (HPLC). The HPLC system was comprised of a Kontron HPLC360 auto sampler, HPLC332 UV-vis absorbance detector and HPLC325 pump. The system was controlled via a Dionex UCI-50 universal chromatography interface using Chromeleon v.6.80 software. The analytical column was a 150 × 4.6 mm Thermo Scientific BDS (base deactivated Silanol) Hypersil column packed with 5 micron ODS (Octadecyl-silica). The mobile phase comprised 25 mM sodium phosphate at pH 3.5 with 0.1% w/v sodium dodecyl sulfate (eluent A) and methanol (eluent B), and a gradient program was used as follows: 0.0 min 30% B, 6.0 min 70% B, 6.1 min 100% B, 7.9 min 100% B , 8.0 min 30% B and 18.0 min 30% B. The flow rate was 0.8 ml min−1, the injection volume was 20 µL and the eluate was monitored at 254 nm. The expected retention time of creatinine was 4.8 min. Electrospun webs were peeled off the collector, and a fixed mass of the sample was added to 50 ml of distilled water and shaken at a constant temperature of 25℃ for 1 hr.
Results and discussion
Electrospinning of PSU in polar binary solvent systems
Table 1 summarizes the binary and ternary solvent systems. The selection of solvents was informed by previous studies of the solubility of PSU and creatinine8,13,17 and by the Hansen theory of solubility.18,19 The solubility parameter (δ) is a numerical value that characterizes the relative solvency behavior of a specific solvent. The concept that solubility is related to the internal energy of solvents and solutes was first introduced by Hildebrand as the square root of the cohesive energy density (CED) of the material. Hansen parameters extended the concept that the total cohesive term and thus the total solubility parameters (δ) of the total Hildebrand value may be divided into the dispersion component (δd), the polar component (δp) and the hydrogen bonding component (δh) as follows
19
Solubility parameters of various solvents and polysulfone (PSU)
D(s–p) = [4(δds − δdp)2 + (δps − δpp)2 + (δhs − δhp)2]1/2
δxs = Hansen component parameter for the solvent.
δxp = Hansen component parameter for the polymer.
Creatinine is highly soluble in water and methanol and among the reported solvents selected for electrospinning of PSU, slightly soluble in DMSO. 8 However, based on Hansen theory, water and methanol are not solvents for PSU (Table 2). The Hansen sphere (D(s–p)) of methanol and water are 17.16 and 36.55 MPa1/2, respectively, which is not within an appropriate range for the dissolution of PSU. The incorporation of water also decreases the overall evaporation rate during electrospinning. 20 Therefore, methanol, which is a solvent for creatinine, was selected as a component in the preparation of PSU binary and ternary solvent systems (Table 1). In some cases, the addition of methanol altered the solvent ratio leading to precipitation of the PSU, but the binary solvent system of 4:1 DMAc:methanol led to PSU dissolution (Table 1) at 80℃.The Hansen sphere (D(s–p)) of DMAc and DMF are 5.50 and7.09 MPa1/2, respectively, which indicates that DMAc is a better solvent for the dissolution of PSU than DMF (Table 2). Furthermore, compared to other solvents (acetone, DMAc and DMF), the distance (D(s–p)) of DMSO to the radius of interaction (R) of PSU was not too high; in other words, DMSO itself was not able to dissolve PSU properly. This characteristic was confirmed in the preliminary results (not shown herein). As a result, binary and ternary solvent systems of acetone, DMAc, DMF and DMSO were also evaluated to improve the electrospinnability of PSU enriched with creatinine (Table 1). The preparation of PSU solutions in binary solvent systems of DMF:methanol (4:1 and 3:2) were hampered due to the precipitation of the polymer during the stirring process (Table 1). Based on Hansen parameters (D(s–p) < 9.40), the solubility of PSU in DMAc is greater than DMF (Table 2). Therefore, all experiments were conducted using DMAc, methanol and DMSO. The solvent ratios were selected based on previous studies.8,13,17,21 Precipitation of PSU occurred in the binary solvent system of 3:2 DMAc:methanol even at a low PSU concentration of 10 wt%. Due to the insolubility of PSU in methanol, the ratio of DMAc:methanol was changed from 3:2 to 4:1.
The suitability of a 4:1 DMAc:methanol system was assessed in terms of the freedom from precipitation during the preparation of the spinning solution and the spinnability of the resulting solution. Spinnability in this context refers to the freedom from needle blockages, the consistency of fiber morphology and the freedom from bead and spindle defects in the web. Therefore in the binary system of 4:1 DMAc:methanol, the PSU concentration was varied from 10–22 wt% (Figure 1(a)–(c)). No fibers were obtained at a concentration of 10 wt% due to a low solution viscosity. As expected, as the polymer concentration increased from 15 wt% to 22 wt%, the electrospun mean fiber diameter increased from 600 nm to 1.06 µm. Morphologically, more uniform fibers free of bead defects were obtained at the highest polymer concentration of 22 wt% (Figure 1(c)). Polymer concentration is known to be one of the most effective variables for controlling morphology and diameter.22–27 While webs containing PSU and creatinine could be successfully produced using a binary solvent system of 4:1 DMAc:methanol (Figure 1(c)), the dissolution of PSU in binary solvents containing either DMAc or DMF with methanol could not be obtained below 80℃ (Table 1).
Scanning electron microscopy (SEM) micrographs showing the effect of solvent systems and the concentration on the structure and morphology of resulting polysulfone (PSU) electrospun webs. Magnification 375–1044×; electrospinning solvents: (a) PSU 15 wt%, N, N-dimethylacetamide (DMAc):methanol (4:1); (b) PSU 18 wt%, DMAc:methanol (4:1); (c) PSU 22 wt%, DMAc:methanol (4:1); (d) PSU 22 wt%, N, N-dimethylformamide (DMF):dimethyl sulfoxide (DMSO) (3:2) and (e) PSU 22 wt%, DMAc:DMSO (13:7).
The limitations of the solvent systems containing methanol were addressed by substituting a polar aprotic solvent (DMSO) for methanol. Creatinine is slightly soluble in DMSO, and based on the Hansen solubility parameters, the distance for DMSO, D(s–p) = 8.5 MPa1/2 is less than the radius of interaction (R < 9.40) of PSU (Table 2). DMSO is a polar aprotic solvent that dissolves both polar and non-polar compounds and is miscible with a range of organic solvents including water. 28 Binary solvent systems of DMF:DMSO (3:2) and DMAc:DMSO (13:7) were found to dissolve PSU and creatinine at room temperature. The ratio of DMAc:DMSO (13:7) has been selected based on the non-precipitation of PSU in the solvent system. In the case of DMAc:DMSO (1:4), satisfactory spinning conditions could not be established, and continuous electrospinning was hampered due to blockage of the nozzle tip. However, electrospun PSU webs were successfully spun from two binary solvent systems (Table 1), specifically DMF:DMSO (3:2) and DMAc:DMSO (13:7) as indicated in Figure 1(d) and (e).
Formation of PSU-creatinine nanofibrous membranes using a binary solvent system
Both DMF:DMSO (3:2) and DMAc:DMSO (13:7) spinning solutions enabled the production of electrospun fiber webs (Figure 1). Electrospinning from DMF:DMSO (3:2) produced a higher mean fiber diameter of 1.1 µm (range: 650 nm–1.90 µm), compared to 630 nm (range: 540–890 nm) for DMAc:DMSO (13:7). The long-term continuous electrospinning of DMF:DMSO (3:2) was partially interrupted by nozzle blockages, whereas DMAc:DMSO (13:7) consistently produced high quality fibers, free from beads and a stable spinning conditions at ambient temperature (Figure 1(e)).
Spinning solutions were prepared of 22 wt% PSU and 2 wt% creatinine in DMAc:DMSO (13:7). Solutions were stirred for 5 hr at ambient temperature. Electrospinning was conducted at 25 kV, a flow rate of 0.004 ml min−1 and a tip to collector distance of 130 mm. The presence of creatinine in the as-spun PSU nanofibers was confirmed by HPLC.
29
The retention time of creatinine was 4.8 min (Figure 2), and an absorption peak was detected in the sample solution which was characteristic of creatinine (Figure 2).
(a) Chromatogram of creatinine (0.1 mg ml -1): creatinine retention time 4.8 min and (b) detection of creatinine in polysulfone (PSU) sub-micron fibers (22 wt% PSU and 2 wt% creatinine in N, N-dimethylacetamide (DMAc):dimethyl sulfoxide (DMSO) (13:7)) after washing in 50 ml of distilled water and shaken at a constant temperature of 25℃ for 1 hr. The mobile phase comprised of 25 mM sodium phosphate pH 3.5 with 0.1% w/v sodium dodecyl sulfate (eluent A) and methanol (eluent B). The injection volume was 20 µl and the eluate was monitored at 254 nm. The retention time of creatinine is 4.8 min.
Successful incorporation of creatinine within the PSU sub-micron fibers was therefore confirmed. SEM micrographs of the PSU-creatinine webs produced from DMAc:DMSO (13:7) are given in Figure 3. The fibers presented cylindrical morphology with diameters in the range 470–870 nm, with a mean of 630 nm.
Scanning electron microscopy (SEM) micrograph of polysulfone- (PSU-)creatinine web produced from a N, N-dimethylacetamide (DMAc):dimethyl sulfoxide (DMSO) (13:7) binary solvent system. Mean fiber diameter = 630 nm; magnification 2000×.
The addition of creatinine molecules to the binary solvent solution resulted in no discernible changes in fiber morphology. The wet stability of the as-spun PSU-creatinine fibers was determined by immersion in distilled water and ethanol for 48 hr. Electrospun webs in the range of 470–870 nm (mean = 630 nm) were carefully peeled off the aluminum collector and immersed in water and ethanol at 25℃. After 48 hr immersion, the samples were removed and dried at room temperature before being placed in the SEM sample chamber. No fiber morphology modifications and swelling were observed after extensive washing in water and ethanol for 48 hr (Figure 4). The immersed fibers were mostly of cylindrical morphology, and the diameters were also in the range of 450–870 nm (mean = 640 nm).
Scanning electron microscopy (SEM) micrograph of polysulfone- (PSU-)creatinine polymer webs produced from N, N-dimethylacetamide (DMAc):dimethyl sulfoxide (DMSO) (13:7) after 48 hr washing in (a) ethanol and (b) water; magnification 500×.
Pore structure of Webs
The porosity of the webs produced from 22 wt% PSU from different solvents of DMAc:methanol (4:1), DMF:DMSO (3:2) and DMAc:DMSO (13:7) was 64–70%. Figure 5 shows typical wet and dry curves obtained by porometry, and Table 3 shows the pore size distributions obtained for PSU webs produced from different solvent systems. The wet curve was measured to determine the pore size; the dry curve is needed for the calculation of the mean flow pore size (MFP), the smallest pores and the gas permeability. The smallest pore is calculated as the pressure (bar) where the dry curve is closest to the wet curve (Figure 5).
Wet and dry curve of polysulfone (PSU) fiber web (22 wt%) obtained from capillary flow porometer, N, N-dimethylacetamide (DMAc):dimethyl sulfoxide (DMSO) (13:7), mean flow pore size (MFP) = 2.71 µm. Mean pore size diameter of polysulfone (PSU) (22 wt%) webs produced from sample A, N, N-dimethylacetamide (DMAc):methanol (4:1); sample B, N, N-dimethylformamide (DMF):dimethyl sulfoxide (DMSO) (3:2) and sample C, DMAc:DMSO (13:7)
The pore structure plays an important role in the filtration behavior of the web. The largest pore (at the bubble point) of 8.8 µm was produced from the binary solvent system of DMF:DMSO (3:2), with the average diameters of fibers equal to 1.1 µm, range: 650 nm–1.90 µm (Table 3). This comparatively large pore size is attributed to the fiber diameter of electrospun nanofibers which potentially affects the mean pore size of the sample. The mean pore size increases with increasing fiber diameter; 30 however, the bubble points obtained using the other binary solvents were of the order of 5 µm. It has been previously reported that PSU membranes with a bubble point of 4.6 µm were able to successfully remove 99% of particles of 7–10.8 µm without any permanent fouling. 14
Conclusions
The aim of this paper was to find a new solvent system that will allow electrospinning of PSU commixed with a highly polar molecule, creatinine, at near ambient temperature. The binary and ternary solvent systems were selected based on the solubility behavior evaluated using Hansen theory. The addition of methanol to the spinning solution, to increase the solubility of creatinine, altered the solvent ratio leading to precipitation of PSU, except in the binary solvent system of DMAc:methanol (4:1). Bead-free, sub-micron fibers were successfully produced from the binary solvent solution of DMAc:methanol (4:1) by electrospinning with fiber diameters ranging between 600 nm–1.05 µm. However, elevated temperature (80℃) was needed to dissolve the PSU polymer, which did not provide the ideal solvent system. A co-solvent system of DMAc:DMSO (13:7) was also found to enable mixing of PSU and creatinine enabling fibers substantially free of structural defects to be produced with diameters in the range 470–870 nm. A mixed binary solvent system of DMF:DMSO (3:2) solution was also compatible with PSU-creatinine fiber production but not on a continuous basis due to nozzle blockage. The presence of creatinine in the as-spun PSU fibers produced by the binary solvent system of DMAc:DMSO (13:7) was confirmed by HPLC. No fiber morphology modifications were observed after extensive washing in water and ethanol for 48 hr, which confirmed the wet stability of the as-spun PSU-creatinine fibers.
Footnotes
Declaration of conflicting interests
The authors declared no potential conflicts of interest with respect to the research, authorship and/or publication of this article.
Funding
The authors received no financial support for the research, authorship and/or publication of this article.
