Dong Jin Woo†
and
S. Kay Obendorf*
Fiber Science, Cornell University, Ithaca, NY 14853, USA. E-mail: sko3@cornell.edu
First published on 21st March 2014
Magnesium oxide nanoparticles (MgO) were embedded in a cellulose acetate fibrous framework to provide self-decontaminating properties against toxic organophosphates. The concept of a co-continuous polymer blend structure coupled with selective polymer dissolution was used to develop electrospun fibres with novel morphology for application in chemical protective materials. An electrospinning solution built from 60:40 acetonitrile–acetone and 15 wt% of 60:40 cellulose acetate–PEO distinct fractions produced fibres that had a degree of continuity of about 0.77 relative to the PEO phase in the cellulose acetate matrix that led to intra-fibre pores with an average diameter of 89 nm, and a surface area of 21.8 m2 g−1. MgO was incorporated into the spinning solution for development of a fibre framework with self-decontamination properties for toxic organophosphates. In 100 min, the MgO-embedded fibres removed 33% of methyl parathion from a hexane solution while fibres with similar morphology and no MgO removed 14%.
In engineering self-contaminating protective materials, inclusion of metal oxides in fibres immobilizes the nanoparticles providing some potential advantage over powders or conglomerated materials. As the reaction between a toxic compound and metal oxide particles occurs on the surface of the crystallites, we previously observed a significant mass transfer limitation when nanoparticles were dispersed throughout the fibre structure.3 This means that modification of the morphology of fibre containing metal oxide particles could enhance reactivity.
Fibres containing continuous pores and channels have been used as sorbents, since they have large surface area.10,11 The interconnected microporous structures in fibres have been achieved based upon co-continuous structure of polymer blends, allowing control of pore size, pore size distribution and morphological change in external surface of fibre.12–16 While several existing techniques such as solvent casting, melt blending, emulsion phase separation, and nonwoven fiber bonding have been used to design a co-continuous blend, in this study, fibres with nanoscale morphologies of interconnected grooves and pores were produced from a co-continuous polymer blend formed in a binary solvent during electrospinning. This fibrous substrate was characterized as a sorbent, adding MgO nanoparticles to the fibre spinning solution to provide enhanced adsorption and degradation of organophosphates such as methyl parathion.
Viscosities of spinning solutions were measured using a TA Instruments AR2000 Advanced Rheometer (New Castle, DE) with cone geometry of 20 mm with a 4° angle and Rheology Advantage Instrument Control AR Version V5.7.2 software. The protocol used an initial temperature of 38 °C and equilibration time of 1 min. Temperature was decreased to 22 °C at the rate of 1 °C min−1 using a shear rate of 10.00 L s−1. Visual turbidity was recorded and used to develop a phase diagram in order to identify the transition region from a single phase to two phases (coexistence).
The degree of continuity is the fraction of a phase that is continuous in the morphological structure and is calculated using the following equation:
φi = (mio − mif)/mio | (1) |
Thermal properties of the electrospun fibres were evaluated using differential scanning calorimeter (DSC 2920; TA Instruments, New Castle, DE). Samples of 4–10 mg were crimped in an aluminum sample pan and scanned from 25 to 300 °C at a rate of 10 °C min−1 under a nitrogen purge (99.99% pure). Thermogravimetric analysis was performed at a heating rate of 10 °C min−1 between 25 and 700 °C in ambient air environment using a TGA 2950; TA Instruments (New Castle, DE).
Brunauer–Emmett–Teller (BET) surface area21 and intra-pore size were determined from nitrogen adsorption isotherm data at 77 K (liquid nitrogen temperature) using Micrometrics analyzer (ASAP 2020, Norcross, GA). Prior to measurement, fibre specimens (50–100 mg) were degassed for at least 12 h under vacuum at ambient temperature. BET surface areas were determined from 9-point adsorption isotherms that were completed using a 0.06–0.2 relative pressure range (p/p0). Pore-size and the distributions were calculated from Barrett–Joyner–Halenda (BJH)22 desorption data in 0.02–0.99 relative pressure range (p/p0).
Degradation of methyl parathion were determined by exposing a 250 mg fibre specimen to 20 mL of a 62.5 mg L−1 methyl parathion–hexane solution with shaking for one of three reaction times (1, 10 and 100 min) using three replications. After reaction, 1.5 mL of the hexane solution was taken with a syringe and filtered by syringe filter with 25 mm diameter consisting of 0.2 μm pore size (Alltech Assoc. Inc., Deerfield, IL) and analyzed by HPLC. The amount of methyl parathion was calculated from the concentration determined by HPLC and original volume; no correction was made for any methyl parathion retained by the syringe filter.
Varying the ratio of the two solvents or polymer in the spinning solution resulted in different fibre diameters (Fig. 1). Fibre diameter increased with increasing polymer concentration and increasing acetone content in the spinning solutions. Increase of fibre diameter with increasing polymer concentration is due to consequentially higher viscosity.29–33 The concentration of a polymer solution determines three important factors for electrospinning: viscosity, surface tension, and electric conductivity. Solution surface tension and viscosity play important roles in determining the range of concentrations from which continuous fibres can be obtained. At low concentrations, beads are formed instead of fibres, and at high concentrations, the formation of continuous fibres is prohibited because of the inability to maintain the flow of the solution at the tip of the needle. The polymer concentration with its corresponding viscosity is known to be one of the most effective variables to control fibre morphology. Increasing the relative amount of acetone to acetonitrile from 40 to 80% resulted in an increase in viscosity (Table 1) and fibre diameter (Fig. 1).
Polymer content (wt%) | Solvent ratio acetonitrile–acetone (w/w) | Viscosity at 22 °C (Pa s) |
---|---|---|
10 | 60:40 | 0.07 |
10 | 20:80 | 0.11 |
15 | 60:40 | 0.24 |
15 | 20:80 | 1.36 |
A phase diagram was constructed with the turbidity data for 60:40 cellulose acetate–PEO using varying ratios of acetonitrile and acetone (Fig. 2). Solutions with high concentrations of acetonitrile resulted in homogeneous single phase solutions while high concentrations of polymer were not soluble. For some solutions near the phase boundary, it was ambiguous whether the specimen was one-phase or two-phase; these were denoted as coexisting. A narrow region with polymer content less than 18 wt% was observed to have a single phase. Solutions close to the phase boundary region which is expected to favor formation of co-continuous structures were selected for electrospinning. Fibres were obtained for 60:40 cellulose acetate–PEO with polymer concentration from 12–18 wt% with weight ratios of acetonitrile–acetone of 30:70, 40:60, 60:40, and 70:30.
Fig. 2 Ternary phase diagram with compositions (wt%) of solutions (solid circle: two-phase solution, hollow square: single-phase solution, hollow triangle: coexistence phase solution). |
Weight ratio of solvents (acetonitrile–acetone) | Fibre mass after water extraction (%) | Degree of continuity of PEO phase |
---|---|---|
a Electrospinning solutions of 60:40 cellulose acetate–PEO at 15 wt% and conditions of 0.08 mL min−1, 15–18 kV, 15 cm. | ||
30:70 | 95.8 | 0.11 |
40:60 | 89.0 | 0.28 |
60:40 | 69.1 | 0.77 |
70:30 | 75.7 | 0.61 |
0:100 | 98.9 | n/a |
Fibres electrospun with 30:70 acetonitrile–acetone exhibited no significant porous structure or surface grooves and had a degree of continuity of only 0.11 (Table 2). This suggests that in the acetone-rich electrospinning solution the 60:40 cellulose–PEO blend was highly miscible resulting in little phase separation of PEO. In addition, the evaporation rate of acetone during electrospinning was rapid allowing little or no phase separation. With 70:30 acetonitrile–acetone, fibres with surface roughness and pores and a degree of continuity of 0.61 were obtained (Fig. 3 and Table 2). These observations agree with those of Megelski et al.11 who reported that electrospinning solutions with relatively low vapor pressure resulted in fibre morphologies with increased surface roughness and pores. Decreased viscosity promotes the development of a finely dispersed structure38 while differences in solubility of the polymer components in the common solvent leads to the formation of interconnected, co-continuous structure.39
Since strongly immiscible behavior in thermal analysis has been shown to relate to matrix-domain dispersed morphology and phase separation of co-continuous blends,26,40 DSC thermal analysis was conducted (Fig. 4). The glass transition temperature (Tg) of cellulose acetate is 198–205 °C, and melting temperature (Tm) is 224–230 °C.17 In the electrospun cellulose acetate fibre, the Tg transition is not obvious while a broad low endothermic peak centered at 224 °C corresponds to Tm. Electrospun PEO fibre showed a strong melting endotherm at 64 °C, and all PEO-containing fibres or film showed this typical melting transition. Different thermal behavior was observed for 60:40 cellulose acetate–PEO fibres electrospun with solvent systems with different ratios of acetonitrile and acetone. Fibres electrospun using 30:70 acetonitrile–acetone exhibited a strong peak at 172 °C between that melting temperatures of cellulose acetate and PEO. In contrast, use of 60:40 acetonitrile–acetone resulted in fibres that exhibited individual peaks at 50 and 220 °C, corresponding to PEO and cellulose acetate, respectively; these conditions produced fibres with the highest degree of continuity of the PEO phase (0.77).
Using 60:40 acetonitrile–acetone, the effect of polymer concentration on fibre morphology was investigated (Fig. 5). Fibres spun from 12 wt% of 60:40 cellulose acetate–PEO had tiny knots and blossom-like structures on their surfaces. Using a polymer concentration of 15 or 18 wt%, fibres with larger diameters and morphologies with grooves and pores were obtained.
After selective dissolution of PEO, the surface area of fibres spun using 12 wt% 60:40 cellulose acetate–PEO was 19.7 m2 g−1 compared to 6.5 m2 g−1 for the 100% cellulose acetate control fibres (Table 3). Furthermore, the fibre spun using 15 wt% polymer had a surface area 21.8 m2 g−1 and average fibre diameter of 1.3 μm. The surface area of this fibre with unique morphology was about three times larger than the control fibre, which if adjusted for fibre diameter would be six to seven times that of the control 100% cellulose acetate fibre with an average fibre diameter of 0.57 μm. The surface area obtained for these fibres with the unique morphology is higher than those reported by other researchers.41,42
Polymer ratio (w/w) | Polymer wt% | Water extracted | BET surface area (m2 g−1) | BJH pore size (nm) | Fibre diameter (μm) |
---|---|---|---|---|---|
100 cellulose acetate | 15 | No | 6.5 | 4.1 | 0.57 ± 0.17 |
60:40 cellulose acetate–PEO | 12 | Yes | 19.7 | 23.3 | 0.55 ± 0.20 |
60:40 cellulose acetate–PEO | 15 | No | 21.8 | 89.0 | 1.33 ± 0.28 |
Based upon an analysis of nitrogen adsorption–desorption isotherms (BET method) shown in Fig. 6, the control cellulose acetate fibres exhibited Type II behavior according to IUPAC classification.21 This physisorption behavior is consistent with that of nonporous materials adsorbents with very small average pore size and distribution and suggests a homogeneous state for the spinning solution. However, the isotherms for fibres electrospun from cellulose acetate–PEO showed Type IV adsorption with hysteresis loops of a Type H2, tending to saturate at high pressures, which means the fibres are associated with capillary condensation taking place in mesopore (2–50 nm). The desorption hysteresis is narrower for the fibre spun from 12 wt% polymer versus the 15 wt% polymer solution (Fig. 6c compared with 6e). This isotherm behavior indicates that the fluffy morphology fibre made using 12 wt% cellulose acetate–PEO has a relatively simple pore structure and a more uniform size distribution (Fig. 6d). In contrast, longer desorption tail in hysteresis of the isotherm (Fig. 6e) of the fibre with unique morphology made using 15 wt% cellulose acetate–PEO suggests a more complex porous structure. BET/BJH measurements show the smallest intra-fibre pore size of 4.1 nm for the control cellulose acetate fibre. The cellulose acetate–PEO fibre from a spin solution with the same polymer concentration had a bimodal pore size distribution as well as the largest and more complex porous structure with the most frequent pore diameter being 89.0 nm. These observation are consistent with porous structures reported by Han et al.27
Fig. 7 MgO-embedded fibre electrospun from 60:40:06 cellulose acetate–PEO–MgO before water extraction. Scale bar is 3 μm. |
Polymer ratio (w/w) | MgO loading | PEO water extracted | Td (°C) at 5% wt loss | Weight residue at 700 °C, (wt%) |
---|---|---|---|---|
100 cellulose acetate | No | No | 289 | 0.9 |
100 cellulose acetate | Yes | No | 297 | 11.2 |
60:40 cellulose acetate–PEO | No | Yes | 290 | 0.7 |
60:40 cellulose acetate–PEO | Yes | Yes | 295 | 9.1 |
Fig. 8 Scheme for methyl parathion degradation in the presence of MgO nanoparticles where [I] is O,O,O-trimethyl phosphoric thiourate, [II] is 4-nitrophenol, and [III] is a degraded and adsorbed compound with PS bond on MgO microcrystalline surface.4 |
Degradation products of O,O,O-trimethyl phosphoric thiourate and 4-nitrophenol were observed in addition to residual methyl parathion after exposure to the MgO-embedded fibrous membranes for 10 and 100 min in a hexane solution. The main degradation product, 4-nitrophenol, has been shown to be transformed into hydroquinone, which is later oxidized to 1,2,4-benzenetriol and then to 5-hydroxymethyl-5H-furfuran-2-one.37 The literature also reports that the organic intermediate species degrade at a slower rate than methyl parathion with mineralization of methyl parathion occurring in 6–8 h. Since our experiment was much shorter (less than 2 h), complete mineralization was not expected.
Methyl parathion is toxic to several target organs, predominately the central nervous system, especially when metabolized to methyl paraoxon which is more toxic than methyl parathion. Neurotoxicity is primarily caused by the inhibition of acetylcholinesterase which results in the accumulation of acetylcholine.45 We did not observe methyl paraoxon when methyl parathion was degraded by MgO-embedded fibres in agreement with our previous research with MgO-embedded fibres.4 The main degradation product of 4-nitrophenol is rated moderately hazardous by WHO while methyl parathion is rated as extremely hazardous. All degradation products that we observed in samples treated for up to 100 min have lower toxicity than methyl parathion. Cleavage of methyl parathion via dearylation to 4-nitrophenol and dimethyl thiophosphoric acid promotes detoxification (Fig. 8).
Amounts of residual methyl parathion for control fibres (S1) and fibres with the unique morphology created by co-continuous structure and selective dissolution (S2) are presented in Fig. 9 and (Table 5). The results confirmed that both MgO-embedded fibres enhanced methyl parathion removal. Overall, MgO-embedded fibre with the unique grooved morphology showed larger decrease of methyl parathion (33.6% removal in 100 min compared to 13.6%) and higher reaction rate than the control MgO-embedded fibres. This difference in performance is believed to be due to the large surface area of the grooved-fibre morphology (21.8 m2 g−1). Furthermore, the pores in the fibre (average intra-fibre pore width: 89 nm) are thought to contribute to the sorption of methyl parathion. Fibres with grooved morphology and no MgO reduced the methyl parathion in the solution after 100 min (7.2%) while no removal was observed for the unloaded control fibre. Results suggest that more than 100 min and/or more than 8 wt% MgO would be required to remove all of the methyl parathion from the solution by destructive adsorption and/or physical adsorption into the fibre pores. Since destructive adsorption by MgO crystallites is stoichiometric, removal of methyl parathion by MgO-embedded fibres will be related to the initiate load of methyl parathion relative to the amount of MgO.
Fibre morphology | Polymer ratio | MgO loaded | Water extracted | Fibre diameter (μm) |
---|---|---|---|---|
Control (S1) | 100 cellulose acetate | No | No | 0.57 ± 0.17 |
Control (S1) | 100 cellulose acetate | Yes | No | 0.86 ± 0.21 |
Grooved (S2) | 60:40 cellulose acetate–PEO | No | Yes | 1.33 ± 0.28 |
Grooved (S2) | 60:40 cellulose acetate–PEO | Yes | Yes | 1.35 ± 0.39 |
Footnote |
† Current address: Physics, Naval Postgraduate School, Monterey, CA 93943, USA. |
This journal is © The Royal Society of Chemistry 2014 |