Jinhao Xua,
Binjie Xin*a,
Zhuoming Chena,
Yan Liub,
Yuansheng Zhenga and
Fuli Zhangc
aSchool of Fashion Engineering, Shanghai University of Engineering Science, Shanghai 201620, China. E-mail: xinbj@sues.edu.cn
bSchool of Chemistry and Chemical Engineering, Shanghai University of Engineering Science, Shanghai 201620, China
cThe Naval Medical I Research Institute, Shanghai 200433, China
First published on 29th May 2019
Directional water transport in garment materials plays a pivotal role in maintaining human thermal and wet comfort. In the present work, a new type of multilayer fibrous mat with the specific function of directional water transport was prepared via the combination of melt-electrospinning and solution-electrospinning. The polypropylene (PP) fibrous layer prepared by melt-electrospinning technology was located in the inner layer (next to the skin), while the polyacrylonitrile-containing hydrophilic nano-silica particles (PAN-SiO2) layer with remarkable hydrophilicity was located in the outer layer, which could effectively transport water to the outer surface of the composites. Treatment of the as-prepared PAN-SiO2/PP with an alkaline aqueous solution of dopamine not only increased the wettability of the PP layer, but also further improved the hydrophilicity of PAN-SiO2. A layer of cotton woven mesh was added between the TPP layer and TPAN-SiO2 to form a sandwich structure in order to accelerate water transport in the bilayered fibrous mats. The directional water transport, mechanical flexibility, and permeability of the prepared multilayered superfine fibrous mat were characterized systematically. The experimental results exhibited that TPAN-SiO2/cotton mesh/TPP exhibited an excellent accumulative one-way transport index (AOTI, 1071%), remarkable overall moisture management capacity (OMMC, 0.88), and reasonably high water vapor transport rate (WVT, 11.6 kg d−1 m−2), indicating it is a promising candidate for the development of novel textile materials for use in the field of sportswear for fast sweat release applications.
Electrospinning is an efficient textile processing technology for most polymers for the manufacture of fibrous membranes of various sizes ranging from nanoscale to microscale.10 Previously, various types of fibrous materials with excellent directional water transport have been prepared by electrospinning technology (shown in Table below).
Name | Characteristic |
---|---|
Trilayered fibrous membranes5 | Continuous, spontaneous, and directional water transport |
Cellulose acetate-based nanofibrous membranes28 | Breathable and colorful |
Nonwoven/Polyacrylonitrile-SiO2 nanofiber composite membranes10 | Potential candidate for fast sweat release applications |
Double-layered membranes constructed of poly(vinylidenefluoride) fibrous layer and nylon-6 nanofibrous layer33 | Promising candidate for developing modern breathable textiles with enhanced moisture management properties such as sportswear |
Unidirectional water-penetration composite of hydrophobic polyurethane and hydrophilic crosslinked poly (vinyl alcohol) fibrous layers1 | An interesting “water diode” film is fabricated via a facile electrospinning technique |
Dual-layer electrospun nanofibrous mats consisting of polyacrylonitrile layer and polystyrene layer with and without interpenetrating nanopores, respectively2 | Tailoring surface hydrophilicity of porous electrospun nanofibers to enhance capillary and push–pull effects for moisture wicking |
Presently, electrospun fibrous membranes can be prepared via solution electrospinning and melt-electrospinning.11,12 The solution-electrospinning process is a method with ordinary operation, and fibers can reach the nano-scale. It is widely used for the development of filtration materials, biomedical materials, flexible sensors and other functional products.13 The melt-electrospinning technology uses a heating syringe to melt and eject the solid polymer, which is subjected to electrostatic force drawing, and then cooled and formed in air. Finally, micron-sized fibers are obtained.14,15 Also, due to its unique characteristic, melt-electrospinning can be used to spin polymers that are difficult to dissolve under normal conditions (PET, PP, PLA, etc.).16–18 In addition, the process of melt-electrospinning does not involve solvents, which prevents the volatilization of toxic solvents from causing negative effects on operators and the environment during the spinning process.4 It also can be widely used in air filtration, water filtration, high-efficiency oil absorption and other fields.19
Herein, a multilayered superfine fibrous mat spun by two-mode electrospinning is reported. The polypropylene (PP) fibrous layer inside the mat was spun via melt-electrospinning, which contacts with human skin directly due to its hydrophobicity. The outer surface was mixture of polypropylene (PAN) nanofibers and hydrophilic silicon dioxide (SiO2) particles prepared by solution electrospinning, which is considered suitable as the outer layer material due to its natural hydrophilic property.20,21 A dopamine alkaline aqueous solution was used to treat the as-prepared bilayered fibrous mats to improve the wettability of the PP side, while the PAN-SiO2 nanofiber membranes could partly be hydrolyzed and the silica particles in it fall off, promoting the water evaporation rate on the surface of the membranes. Meanwhile, cotton mesh was specially added between the inner and outer layers to accelerate water transport and endow the material with outstanding mechanical properties.22 Schemes 1 and 2 illustrate the complete preparation process and performance mechanism of the treated PAN-SiO2/PP (TPAN-SiO2/TPP) and treated PAN-SiO2/cotton mesh/PP (TPAN-SiO2/cotton mesh/TPP), respectively.
The spinning solution (100 g) comprised of silica nanoparticles (SiO2 NP) concentration (10 wt% relative to polymer) and polyacrylonitrile (PAN, 12 wt%) was obtained by dissolving the powder reactants in dimethylformamide (DMF) solvent following by magnetic stirring for 8 h. The mixed and uniform solution was electrospun on the surface of PP and cotton mesh-PP by the needle (diameter: 0.3 mm) on an RES-001 Rotary Dynamic Electrospinning Device at a fixed feeding rate of 0.002 mm s−1. A high direct current voltage of 20 kV was applied to the needle tip. The fibrous nanofibers were collected on a grounded metallic rotating roller at the same rotation rate (45 rpm) covered by PP, cotton mesh-PP, and the needle tip-to-collector distance was maintained at 15 cm. The syringing was conducted in a fixed mode for 3 h at room temperature and 45 ± 3% relative humidity.
Fourier transform infrared spectroscopy (FTIR) was conducted on a Spectrum Two spectrometer to examine the molecular structure and chemical information of the different treatment time PAN-SiO2 and PP samples before and after treatment (PerKin Elmer Inc., USA).
The pore size and pore size distribution of the fibrous membranes were analyzed using a capillary flow porometer (POROLUX 100 FM, Promet Co., Ltd., GER).
The thermal mass loss was investigated using a thermogravimetric analyzer (TGA4000, PerKin Elmer Inc., USA) from 30 °C to 800 °C at a heating rate of 30 °C min−1, which showed the amount of SiO2 in the treated PAN-SiO2 fibrous membranes.
The contact angles of droplets (5 μL) were measured using a contact angle tester (Beijing Jinshengxin Testing Instrument Ltd., China).
The thickness of each layer of the composite mat was measured using a fabric thickness gauge by applying a certain pressure (500 g).
A moisture management tester (MMT, SDL ATLAS, Ltd., China) was used to measure the directional water transport performance of the mats. During the test, the sample was placed between two arrays of electric resistance sensors. The transfusion tube in the sensors dripped a fixed concentration of saline water onto the fibrous mats. The probe of the sensors tested the resistance between different rings to reflect the absorption and diffusion of the liquid in the fibrous mats by the change in resistance. The accumulative one-way transport index (AOTI) and over moisture management capacity (OMMC) were calculated as follows:
![]() | (1) |
OMMC = 0.25BAR + 0.5AOTI + 0.25BSS | (2) |
The tensile strength test was based on GB/T3923.1-2013, with modification. The samples were examined using a testing machine (YG006, China) under a fixed stretching speed of 100 mm min−1. The dimensions are fixed parameters (50 × 150 mm) and the distance gauge was set to 100 mm.
The water vapor transmission rate test was based on GB/21655-2008, with modification. Samples were cut into fixed sizes (100 mm × 100 mm), and suspended naturally after wetting with water droplets (0.2 g). The mass of the samples was measured every 5 min.
The wicking height test was based on GB/21655-2008, with modification. The samples were cut into strips (20 mm wide) and dipped into distilled water, and the wicking height was recorded every 2 min.
The drape coefficient and blending length were measured using a YG811 fabric drape tester and FAST-2 bending tester, respectively, followed a reported procedure.23,30 The drape coefficient was calculated using the following formula:
![]() | (3) |
Also, the drape stiffness was calculated using the following formula:
BS = 9.81 × 10−8WLB3 | (4) |
The air permeability test was conducted using an automatic permeability meter (YG461E-III, Ningbo Textile Instruments Ltd., China).
The moisture permeability was tested according to GB/21655-2008, and the moisture permeability was calculated using the following formula:
![]() | (5) |
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Scheme 3 Illustration of the hydrolysis of the PAN-SiO2 membrane in alkaline aqueous solution of dopamine. |
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Fig. 1 Microscopic structure of PAN-SiO2 fiber membranes with different treatment times: (a) 0 h, (b) 0.5 h, (c) 1 h, and (d) 1.5 h. |
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Fig. 2 Pore size distribution of the PAN-SiO2 fibrous membranes after various alkali treatment times of (a) 0, (b) 0.5, (c) 1 and (d) 1.5 h. |
Sample | Td (°C) | α (%) |
---|---|---|
a Td the thermal decomposition temperature at the maximum weight loss rate of material. α weight residue at 800 °C. | ||
PAN-SiO2 | 321.6 | 48.5 |
PAN-SiO2-0.5 | 326.1 | 43.5 |
PAN-SiO2-1 | 326.3 | 43.4 |
PAN-SiO2-1.5 | 326.5 | 43.3 |
PAN | 324.3 | 39.6 |
The existence of nitrile groups and amide bonds in PAN-SiO2 nanofibers caused the nanofibers with a rough surface have certain hydrophilic properties. With an increase in the treatment time of the nanofibers in alkaline aqueous solution of dopamine, the wicking height (Fig. 4a) of the nanofibers increased correspondingly, which indicates that the hydrophilicity of the nanofibers was further improved under the action of the stronger hydrophilic chemical groups on the surface and hierarchical micro–nanoscale roughness.5,20,26 When the treatment time was extended to 2 h, the wicking height tended to drop, which is attributed to the increase in the pore size as the fibers became thinner, weakening the wicking effect of the materials (FS 3†).
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Fig. 4 Wicking height (a), water evaporation rate (b), and apparent WCA of PAN-SiO2 (c) with different treatment times. |
It was observed that the wicking height reached about 10 cm when the PAN-SiO2 nanofiber membrane was treated in the alkaline aqueous solution of dopamine for 1.5 h; thus, the optimum treatment time for the PAN-SiO2 nanofiber membrane was fixed at 1.5 h in subsequent experiments. Simultaneously, the water evaporation rate (Fig. 4b) increased significantly with an increase in the treatment time, indicating the quick drying property of the membranes, which is attributed to the wider wetting area of the hydrophilic nanofiber membrane.25,27
Fig. 4c depicts the apparent water contact angle of a droplet on the surface of PAN-SiO2 nanofibers with different treatment times. The water absorption times for TPAN-SiO2-0.5, TPAN-SiO2-1, TPAN-SiO2-1.5 had no significant difference. Nevertheless, the WCA of PAN-SiO2 was different from that of the other samples, and the water droplets could be absorbed and diffused completely by the nanofiber membrane after 13 s. This indicated that the hydrophilicity of the PAN nanofibers was enhanced due to the hydrophilic SiO2 nanoparticles (PAN-SiO2). Thus, the nanofiber membranes treated by dopamine alkaline solution contained hydrophilic groups on their surface, and the original hydrophilic SiO2 particles did not completely fall off and still existed, leading to a further improvement in the water absorption on the surface of the membrane.24 At the same time, the wettability of the PP layer was also improved in alkali solution of dopamine (FS 4†).
Fig. 6a and b demonstrates the directional water transport of PAN-SiO2/PP and TPAN-SiO2/TPP, which was quantitatively measured using a liquid moisture management tester (MMT). 0.2 g of saltwater was continuously dropped on the surface of the composite fibrous mats for 120 s. The blue line in the figure represents the relative water content at the top of the mat, while the red line represents the water content at the bottom.
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Fig. 6 MMT results of the PAN-SiO2/PP bilayered fibrous mats with (a) 0 and (b) 1.5 h treatment time. |
The resultant AOTI value for PAN-SiO2/PP and TPAN-SiO2/TPP were −852% and 330%, respectively. The water transport behavior was promoted after treatment in alkaline aqueous solution of dopamine due to the improvement in the wettability of the treated PP fibers. The observed images show that when a saltwater droplet was dropped on the PAN-SiO2/PP, the majority of water stayed on the surface of the PP layer and hardly transported to the opposite side. This is because the surface energy was so small that the PP layer was endowed with strong hydrophobic property; hence, the water droplet could not contact the hydrophilic layer (PAN-SiO2) and pulled out by capillary. However, the water content at the bottom was significantly larger than that at the top when a certain amount of water was dropped on TPAN-SiO2/TPP. Initially, the water content at the top increased faster than that at the bottom, and reached the maximum at the point of 10 s. This is attributed to the relatively strong initial hydrophobic force on the TPP side, which slowed the downward transport of water droplets. The water content at the bottom of the layer increased steadily with time and exceeded that at the top at the end of 37 s owing to the water being pulled out by the TPAN-SiO2 layer under the remarkable wicking action, which accelerated the rate of wetting in the bottom area. The bottom water content did not increase significantly after 80 s, and remained at a stable level. Nevertheless, when the composite mat was reversed and the saltwater droplet was added to the TPP-SiO2 side, all the water accumulated at the top without transporting downwards, making the bottom hardly wetted (FS 5a†).
When a suitable amount transparent blue ink droplets (35 μL) was on the TPP side, it was observed that the water was quickly transported from the TPP layer to the opposite side (Fig. 7a and b), showing the excellent wettability on the TPP side and capillary force on the TPAN-SiO2 side. Also, it was observed that the water spreading area on the TPP side was small, because of a large amount of water was absorbed by TPAN-SiO2 and diffused along the transverse direction. Thus, the experimental results prove that TPP has decent water transport ability and did not absorb the water, which meets the requirements of quick drying of inner layer to ensure thermal and humid comfort for the human body. TPAN-SiO2 had remarkable wicking ability, and it could pull water out quickly and accelerate the rate of water transport. However, when water was dropped in the opposite direction (Fig. 7c and d), water accumulated on the surface of TPAN-SiO2 and diffused rapidly along the transverse plane, while only a small amount of water was transported to the other side; thus, most areas of the TPP side remained dry. This phenomenon intuitively demonstrates that TPAN-SiO2/TPP has outstanding directional water transport.
Sample | Sample ID | Average thickness (mm) |
---|---|---|
Single-layer sample | TPAN-SiO2 | 0.074 |
Cotton mesh | 0.33 ± 0.02 | |
TPP-0.5 | 0.11 ± 0.01 | |
TPP-1 | 0.34 ± 0.03 | |
TPP-1.5 | 0.54 ± 0.03 | |
TPP-2 | 0.71 ± 0.04 | |
Multi-layer sample | TPAN-SiO2/cotton mesh/TPP-0.5 | 0.52 ± 0.03 |
TPAN-SiO2/cotton mesh/TPP-1 | 0.74 ± 0.01 | |
TPAN-SiO2/cotton mesh/TPP-1.5 | 0.93 ± 0.01 | |
TPAN-SiO2/cotton mesh/TPP-2 | 1.15 ± 0.03 |
Fig. 8a–d present the water transport behavior and quantitative analysis of the amount of water retained in the top and bottom layers of TPAN-SiO2/cotton mesh/TPP with various thicknesses. The resultant AOTI values for the obtained multilayered superfine fibrous mats were 861%, 1071%, 841%, and 352%. The water content in the TPP layer in TPAN-SiO2/cotton mesh/TPP-1 was almost zero and the hydrophilic layers of all the samples were completely wetted by water after the cotton mesh was sandwiched, which indicate the cotton mesh acts as a transfer layer to accelerate water transport.
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Fig. 8 MMT results for the TPAN-SiO2/cotton mesh/TPP with the 0.5 h (a), 1 h (b), 1.5 h (c), 2 h (d) melt-electrospinning time. |
When the time of melt-spinning was 0.5 h, the thickness of the PP layer was 0.11 ± 0.01 mm. At this time, the water droplet experienced a weaker hydrophobic force because the PP layer was relatively thin. Thus, the water droplet could easily pass through the hydrophobic layer and be absorbed by the hydrophilic side. However, the water droplet easily diffused transversely under the action of the cotton mesh in this case, making the PP layer wetted and affecting the directional water transport of the material, as shown in Fig. 8a. When the spinning time was extended to 1 h, the thickness of the PP layer reached 0.34 ± 0.03 mm. The water droplets could be absorbed by the outer layer and the inner layer kept the dry state for 120 s, showing an excellent water transport effect, as shown in Fig. 8b. Moreover, the composites still exhibited an excellent wearability performance (FS 6 and FS 8†).35 Continuous prolongation of the spinning time to 1.5 h and 2 h caused the thickness of the PP layer to increase constantly. The water droplet was subjected to a greater hydrophobic force in the inner layer, which limited the transport of water in the material, thus affecting the overall performance of the directional water transport (Fig. 8c and d, respectively).
Fig. 9b depicts the mechanism of directional water transport in the multilayered superfine fibrous mat. When the water droplet was dropped on the hydrophobic side, it still retained a Wenzel–Cassie state subjected to two forces in opposite directions, hydrostatic pressure (HP) and hydrophobic force (HF), which is the same as mechanism in the bilayered fibrous mats. When the water droplet moved downward, it would be continuously attracted by the capillary force (CF1 and CF2) provided by the cotton mesh and TPAN-SiO2 successively, resulting in progressive wettability to speed up the water droplet transport to the opposite side, thus increasing the diffusion area of water on the hydrophilic side, as shown in the inserted images in Fig. 6 and 8. On the other hand, when the water droplet was on the hydrophilic layer side, it would be absorbed rapidly by the cotton mesh and TPAN-SiO2 and diffuse horizontally. When water droplets contacted the TPP layer, they suffered from hydrophobic force in the upward direction, preventing the block inner layer from being wetted. Interestingly, insignificant areas of the inner layer in TPAN-SiO2/cotton mesh/TPP were wetted by water due to the close combination of PP fibers and cotton mesh under the action of electrostatic force (FS 5b†), but large areas remained dry in the TPP layer.
Interestingly, in during the experiment, we found that when spinning the PP fiber layer by melt-electrospinning with cotton mesh as the substrate, the PP fibers and cotton yarn were attached relatively close due to the electrostatic force interaction between them. The cellulose fiber also had good hydrophilicity, which meets the requirement of directional water transport. Thus, we will subsequently conduct in-depth research on this material.
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c9ra00996e |
This journal is © The Royal Society of Chemistry 2019 |