Abstract
The dye production and its use in textile and related industries resulted in discharge of dye to wastewater. Adsorption for color removal is known as equilibrium separation process, and the resultant decolorization is influenced by physicochemical factors such as adsorbent surface area. The nanofiber membranes prepared by the electrospinning method have controllable nanofiber diameter and pore size distribution (PSD) with a high surface area to volume or mass ratio. In this study, polyvinyl alcohol (PVA) nanofibrous membranes were prepared by the electrospinning method at different collection times such as 3, 5 and 10 h and heat fixated at 130, 150 and 170°C for 10 min, and then, the adsorption capability of PVA nanofiber membranes for Reactive Red 141 from aqueous solution was investigated. In order to make PVA nanofibers stable to water, the nanofibrous membranes were chemically cross-linked by a polycarboxylic acid (1,2,3,4 butanetetracarboxylic acid (BTCA)). PVA nanofibrous membranes were characterized by scanning electron microscopy, thermogravimetric analysis, swelling tests and pore size analysis. The results indicated that BTCA crosslinking improved the thermal and water stability of the nanofibrous structure but has no significant effect on the pore sizes of the membranes. Adsorption of Reactive Red 141 was studied by the batch technique, and it was observed that PVA nanofibers removed approximately >80% of the dye.
1 Introduction
The world dyes and pigments market was estimated at USD 30.42 billion in 2016 [1]. More than 100,000 commercial dyes are available with over 700,000 tons of production annually [2] of which 50% are textile dyes [3]. The dye production and its use in textile and related industries resulted in discharge of dyes to wastewater. It is estimated that a loss of 1–2% in dye production and 1–10% in use and in total 10–15% of the dyes are discharged as effluent from these industries [2, 4, 5]. Wastewater from the textile dyeing process contains approximately 8–20% dyes of the total pollution load due to incomplete exhaustion of the dyes [2, 6]. Moreover, it is known that more than half of the market size belongs to reactive dyes [1]. In reactive dyeing, unfixed or hydrolyzed reactive dyes have to be washed off thoroughly in order to achieve the desired superior wet fastness. The major cost of a reactive dyeing process could be attributed to the washing-off stages [7]. The main problem about reactive dye effluent is that reactive dyes have very small tendency of being absorbed on the sludge due to their high solubility in water [8]. As a result, they pass through the purification plant and are released into the environment. Thus, lots of researches have been undertaken in order to develop an effective treatment process for color removal of reactive dyes.
A wide range of technologies could be used for color removal of the synthetic dyes from wastewaters to decrease their impact on the environment. These technologies could be divided into three categories such as chemical, biological and physical. Physical methods that include adsorption, ion exchange, filtration and membrane-filtration processes (nanofiltration, reverse osmosis and electrodialysis) are widely used in industry because of their dye removal potentials and low operating costs [2]. Among these techniques, adsorption is known as equilibrium separation process, and generally, it does not result in the formation of harmful substances [9,10,11]. Adsorption has many advantages such as low initial cost, flexibility and simplicity of design, ease of operation and insensitivity to toxic pollutants. Adsorption and resultant decolorization are influenced by physicochemical factors such as dye/adsorbent ratio, adsorbent surface area, particle size, temperature, pH, and contact time.
Adsorption occurs by the interaction between the adsorbate and the molecules in the fluid phase. There are two kinds of forces that bring about to either physical adsorption (physisorption) or chemical adsorption (chemisorption) [12]. Physical adsorption occurs between the adsorbate and the adsorbent reversibly via weak interactions, such as Van der Waals interactions, hydrogen bonding and dipole–dipole interaction. Chemical adsorption occurs irreversibly via strong interactions, such as covalent and ionic bond formation, between the adsorbate and the adsorbent [2]. The attractive forces between the adsorbent and the adsorbate are influenced by the properties of the adsorbent such as structure, surface area, chemical nature and polarity of the adsorbent [13].
Activated carbon [11, 12], clay [14], biomass [15], agricultural solid wastes [16] and nanofibers [14, 15] have generally been used as adsorbents in the adsorption studies. Among these adsorbents, the nanofiber membranes prepared by the electrospinning method have unique properties such as controllable nanofiber diameter, PSD and orientation at a lower cost. The process has attracted a great deal of attention due to its relative ease of use, adaptability [16, 17], lots of possibilities for surface functionalization [18, 19] with a high surface area to volume or mass ratio, small interfibrous pore size and high porosity [17, 20, 21]. These properties have led electrospun nanofiber membranes to be used for the removal of heavy metal ions [22,23,24] and dye molecules from textile wastewater [25, 26].
A wide variety of polymers such as polyethylene oxide [13], chitosan [10, 27], polyacrylonitrile [28], cellulose acetate [29] and polyvinyl alcohol (PVA) [28,29,30] have been used in the studies of wastewater treatments. Apart from these studies, in the present contribution, to the best of authors’ knowledge, porosity comparison of the PVA nanofibers and the effect of fixation temperature and collection period on chemically cross-linked and water-stable PVA nanofibers have been investigated for their reactive dye removal from wastewater for the first time.
PVA is a water-soluble polyhydroxy polymer and has excellent chemical resistance and physical properties along with complete biodegradability, which leads to broad practical applications. In the case of colored textile wastewater, these membranes can be used for both filtration and dye adsorption purposes, which allows the removal of submicron particles and as well as the removal of color from wastewater. PVA nanofiber mats could be prepared by the electrospinning of the aqueous PVA solutions and could be cross-linked with chemical crosslinking agents [31]. In this study, to make PVA nanofibers stable to water and decrease their swelling characteristics in water, they were chemically cross-linked by a polycarboxylic acid (1,2,3,4 butanetetracarboxylic acid (BTCA)). The effects of heat fixation (130, 150 and 170°C) and collection period on adsorption capacities of PVA and BTCA cross-linked PVA nanofibers were compared.
Most of industrial adsorbents have large specific surface areas and are therefore highly porous or consist of very fine particles [12]. Nanofiber-based mediums have low basis weight, high permeability and small pore size that make them also appropriate for a wide range of applications. In order to compare the porosity of produced nanofiber membranes, the pore size measurement performed for 3, 5 and 10 h collected neat-PVA and PVA−BTCA nanofiber membranes. The produced PVA nanofiber membranes were finally evaluated for the color removal of Reactive Red 141 from aqueous solution.
2 Experimental
2.1 Materials
PVA with an average molecular weight of 125,000 g/mol, BTCA, sodium hypophosphite monohydrate: (NaPO2H2·H2O), sodium sulfate (Na2SO4) and sodium carbonate (Na2CO3) were purchased from Sigma Aldrich Chemical Company. The dye, C.I. Reactive Red 141, was supplied from DyStar and used as received. The chemical structure of the dye is illustrated in Figure 1.
![Figure 1 Chemical structure of Reactive Red 141 [8].](/document/doi/10.2478/aut-2019-0040/asset/graphic/j_aut-2019-0040_fig_001.jpg)
Chemical structure of Reactive Red 141 [8].
2.2 The preparation of electrospinning solutions
A weighed amount of PVA was dissolved in distilled water at 100°C to prepare an aqueous PVA stock solution at a fixed concentration of 10% w/w. BTCA as a crosslinking agent was selected to be 5% (w/wpolymer) and was directly added into the spinning solution with sodium hypophosphite monohydrate as a catalyst in the ratio of 2:1 (w/w) followed by stirring for 15 min. As a control, neat-PVA nanofibers were also prepared by electrospinning.
2.3 Electrospinning
Electrospinning of the polymer solutions was carried out by a setup consisting of a syringe (10 ml) with a stainless steel needle (22 gauges and flat tip), a ground electrode and a high-voltage supply (Simco, MP Series CM5 30 P, Charging Generator Output 30 kV DC). A grounded rotating metal drum collector covered by a 90 mesh of plain weave monofilament of 100% polyester screen mesh fabric was used as deposition material. Neat-PVA and PVA−BTCA solutions were electrospun for 3, 5 and 10 h. After electrospinning, the nanofibers were heat fixated at different temperatures such as 130, 150 and 170°C for 10 min and coded as PVA-130, PVA-150, PVA-170, PVA−BTCA-130, PVA−BTCA-150 and PVA−BTCA-170. All electrospinning experiments were performed at room temperature (22 ± 2°C), where the relative humidity was 22–40%.
2.4 Thermogravimetric analysis (TGA) of nanofibrous mats
TGA (Perkin Elmer TGA-4000) of PVA and PVA−BTCA cross-linked nanofibers were carried out by heating samples from 25 to 600°C at a rate of 10°C/min under continuous nitrogen purge at the rate of 20 ml/min.
2.5 Scanning electron microscope (SEM) analysis
The electrospun nanofibers were sputtered by Quorum Q150R S ion sputtering device with a thin layer of gold prior to SEM observation. The morphology of the nanofibers was analyzed by an SEM (Phenom G2 pro).
2.6 Measurement of thickness, weight per square meter and fiber diameters
The thicknesses of the nanofiber mats were measured by Mitutoyo digital micrometer at 0.01 mm accuracy. Weights of nanofiber mats were calculated from the weights of small rectangular pieces. A total of eight and three measurements were carried out from the different parts of each sample for thickness and weight, respectively. The mean diameter of the resultant fibers was calculated from measurements on SEM images of ×10,000 magnification by using ImageJ program. Approximately 50 measurements were carried out from the different parts of PVA nanofiber samples. Measurements of all thicknesses, weights and fiber diameters were expressed as mean ± SD.
2.7 Swelling and weight loss of nanofibrous mats
Swelling of the neat-PVA and PVA−BTCA electrospun nanofiber mats was measured upon exposure in distilled water for 24 h. The samples were removed from the water and carefully blotted with tissue paper to remove the excess from the surface. The degree of swelling due to the water uptake was determined, and weight loss was calculated at the end after drying for 4 h at 70°C in an oven. The percentages of degree of swelling and weight loss were calculated as follows [32]:
and
where M was the weight of each nanofiber mat sample upon exposure in distilled water for 24 h, Md was the weight of the PVA nanofibers after swelling and subsequent drying and Mi was the initial weight of the sample.
2.8 Pore size measurements
The pore size measurements of the PVA nanofiber mats were measured by capillary flow porometry (Porolux 1000, Germany). All samples were wetted by a wetting liquid with a low surface tension of 16 dyne/cm before the measurements. Mean flow pore size (MFP), first bubble point (FBP) and PSD were measured by the wet-up/dry-up method.
2.9 Adsorption experiments
Since the reactive dyes are the most used dye class in the textile industry, the neat-PVA and PVA−BTCA nanofiber mats were used for the adsorption of a commercial reactive dye Reactive Red 141. Na2SO4 and Na2CO3 were added to the adsorption solution in order to simulate the dyeing condition. The kinetic studies were carried out in a 15 ml test tube containing 10 mg adsorbent and 10 ml of the adsorption solution with 45 g/l Na2SO4, 10 g/l Na2CO3 and 85 mg/l dye concentrations at pH 10.5–11. These tubes were stirred on an orbital shaker (Nüve, ST 402) at 25°C over a time interval of 0–48 h. The residual dye concentration in the liquid was analyzed using a UV–Vis spectrophotometer (Perkin Elmer Lambda 25) at 518 nm. The data were used to calculate the adsorption capacity (mg/g), qe, of the adsorbent. The dye concentration on the adsorbent surface at equilibrium was calculated by
where C0 is the initial dye concentration in the liquid phase (mg/l), Ce the equilibrium dye concentration (mg/l), V the total volume of dye solution used (l) and m the mass of adsorbent used (g).
2.10 Adsorption kinetics
Two of the most frequently used kinetic models that are the pseudo-first-order and the pseudo-second-order kinetic models were used for the characterization of the adsorption studies.
The pseudo-first-order kinetic model is given by the following equation:
By taking qt=0 at t=0 and qt=qt at time t, the integrated form of Equation 4 becomes
where qt is the amount of adsorbed dye at time t and k1 is the rate constant of first-order adsorption. The parameters of the equation can be obtained from the linear plot of ln(qe-qt) versus t.
The pseudo-second-order kinetic model is given by the following equation:
where k2 is the pseudo-second-order rate constant of adsorption. As in Equation 4, by taking qt=0 at t=0 and qt=qt at time t, the integrated form of Equation 6 becomes
The plot of t/q versus t gives a straight line with a slope of
3 Results and discussion
3.1 TGA of heat-fixated neat and BTCA cross-linked electrospun PVA nanofibers
In Figures 2–4, the TGA thermograms of 10 h produced neat-PVA and heat-fixated PVA nanofibers with and without BTCA are given according to fixation temperature. In these curves, the electrospun neat-PVA nanofibers lost ~7% mass at temperatures up to 100°C due to the evaporation of absorbed moisture. The decomposition of neat-PVA began around 270°C and lost half of its mass at 330°C, leaving merely ~2% residue at 600°C. Neat-PVA nanofibers had two degradation steps: the elimination reactions started at ~225°C and the breakdown of the polymer backbone (mostly chain-scission reactions) started at ~374°C as a second stage (residue weight: ~83% and ~28%, respectively) (Table 1) [33]. The temperatures of elimination reactions were approximately at 281, 269 and 262°C and the chain-scission reactions were approximately at 477, 468 and 461°C for PVA-130, PVA-150 and PVA-170 nanofibers, respectively. The starting point of elimination reaction almost stayed same, but heat fixation significantly increased the starting temperature of chain-scission reaction due to self-crosslinking with heat. This showed that heat crosslinking had a significant effect on chain scission. After the second stage, these nanofibers showed residue weight of approximately 6–9%. However, the final residue weight at 600°C was not affected from sole heat fixation. For PVA–BTCA-130, PVA–BTCA-150 and PVA–BTCA-170 nanofibers, elimination reactions started at approximately 225, 237 and 223°C and chain-scission reactions started at approximately 352, 352 and 325°C, leaving 46, 46 and 51% residue weight, respectively. These results confirm that an increase in thermal stability is a direct consequence of crosslinking with BTCA, and when compared to BTCA crosslinking is more effective than heat fixation self-crosslinking.

TGA thermograms of 10 h produced neat-PVA, PVA-130 and PVA–BTCA-130 nanofibers.

TGA thermograms of 10 h produced neat-PVA, PVA-150 and PVA–BTCA-150 nanofibers.

TGA thermograms of 10 h collected neat-PVA, PVA-170 and PVA–BTCA-170 nanofibers.
Weight % of the electrospun neat-PVA and 130, 150 and 170°C heat-fixated PVA and PVA−BTCA nanofibers at given temperatures according to the TGA analyses
First stage | Second stage | 600°C Residue (% weight) | |||
---|---|---|---|---|---|
Temperature (°C) | Residue (%weight) | Temperature (°C) | Residue (%weight) | ||
Neat-PVA | 225 | 89.21 | 374 | 28.76 | 2.38 |
PVA-130 | 281 | 90.14 | 477 | 8.59 | 0.18 |
PVA-150 | 269 | 91.87 | 468 | 6.12 | 0.60 |
PVA-170 | 262 | 90.83 | 461 | 9.26 | 2.38 |
PVA–BTCA-130 | 225 | 90.55 | 352 | 46.10 | 14.05 |
PVA–BTCA-150 | 237 | 89.91 | 352 | 46.10 | 17.26 |
PVA–BTCA-170 | 223 | 90.86 | 325 | 50.94 | 8.36 |
3.2 SEM images of PVA and PVA−BTCA nanofibers
The surface morphology of electrospun nanofibers of neat-PVA and PVA−BTCA was investigated by SEM imaging. Bead free, uniform PVA and PVA−BTCA nanofibers were produced (Figure 5). Mean fiber diameters of the neat-PVA and PVA− BTCA nanofibers were approximately 328.9 and 272.36 nm, respectively, and as expected, any change in nanofiber diameters was not observed depending on the collection time. Differences in the fiber diameters were analyzed by one-way ANOVA. It was observed that the difference between the neat-PVA and PVA−BTCA nanofiber diameters was statistically significant (p < 0.05). PVA−BTCA nanofibers were thinner than PVA nanofibers due to the conductivity of the BTCA-added solutions. The addition of BTCA significantly increases the solution conductivity because of the acidic nature [34].

SEM images of (a) neat-PVA and (b) PVA−BTCA nanofibers.
3.3 Thickness and weight per square meter of the neat-PVA and PVA−BTCA nanofibers
Table 2 lists the mean thickness and weight of the neat-PVA and PVA−BTCA nanofibers. Heat fixation did not have an effect on these data; thus, they were given according to the collection periods. As expected, the thickness and weight of the nanofiber mats were significantly affected by the collection period, and the thickness of the neat-PVA nanofiber mats was more than that of the PVA−BTCA nanofibers due to their thicker nanofiber diameter.
Thickness and weight of the electrospun neat-PVA and PVA− BTCA nanofibers
Mean thickness (mm) ± SD | Mean weight (g/m2) ± SD | |
---|---|---|
PVA – 3 h | 0.076 ± 0.020 | 17.84 ± 0.62 |
PVA –5 h | 0.149 ± 0.025 | 34.32 ± 3.89 |
PVA –10 h | 0.180 ± 0.024 | 38.80 ± 1.31 |
PVA−BTCA – 3 h | 0.029 ± 0.010 | 8.99 ± 1.10 |
PVA−BTCA – 5 h | 0.085 ± 0.020 | 20.92 ± 2.33 |
PVA−BTCA – 10 h | 0.140 ± 0.020 | 28.65 ± 5.92 |
3.4 Swelling and weight loss of nanofibrous mats
Swelling and weight loss of the neat−PVA and PVA−BTCA nanofibers are given in Figure 6 according to the heat fixation temperatures. Without BTCA, the degree of swelling of PVA nanofibers was : was ~4000% for the heat fixation temperatures of 130 and 150°C, while the percentage of weight loss was as much as ~82–96%. However, when the heat fixation temperature was increased to 170°C, swelling of the nanofibers significantly decreased to 690% and weight loss to 15% due to the self-crosslinking of PVA with heat [32]. BTCA crosslinking led to a significant decrease in the degree of swelling at 150°C. It was ~650%, and weight loss of the PVA–BTCA-150 nanofibers was 8%. Slight swelling of the nanofibrous structure occurred with negligible weight loss. However, for PVA–BTCA-130 nanofibers, swelling of the mats was ~2500%, while weight loss was ~41%, which means 130°C was not enough for crosslinking. Swelling and weight loss of PVA–BTCA-170 nanofibers were close to those of PVA-150 nanofibers and showed that they were cross-linked properly.

Swelling and weight loss of 10 h collected neat-PVA and PVA−BTCA nanofibers after heat fixation at 130, 150 and 170°C.
3.5 Pore size analysis
To compare the pore size of the neat-PVA and PVA−BTCA nanofibers mats according to their collection period, the vertical capillary method was performed by capillary flow porometry. It provides a better understanding of water penetration on the surface since this method takes the whole structure of the nanofibers into account [35].
The FBP, the MFP and the smallest pore size are given in Table 3. A decrease in the mean nanofiber diameter of PVA−BTCA nanofibers did not cause a significant effect on the pore sizes; they were close to that of the neat−PVA nanofibers. The FBP was in the range of 2.01–2.45 and 2.05–2.34, and the MFP was in the range of 1.05–1.33 and 1.26–1.32 for the neat-PVA and PVA−BTCA nanofibers, respectively. The effect of the electrospun membrane thickness on the pore size can be explained by depositing more fibers on the substrate, which results in smaller pores when other variables (such as fiber diameter and fiber length) are kept constant. However, the mean pore size reached an asymptotic level with the increase in mat thickness [36]. In our case, the membrane thicknesses of both the neat−PVA and PVA−BTCA nanofibers were too high and did not play an important role in reducing the pore size. There was not any statistical difference (p < 0.05). According to these results, to achieve smaller pore sizes, there is no need to extent the collection period to 5 or 10 h. In all, 3 h of collections with thickness of 0.029–0.079 mm is enough for approximately 1 μm MFP.
Pore size measurement results of the electrospun neat-PVA and PVA−BTCA nanofibers
FBP (μm) | MFP (μm) | Smallest pore size (μm) | |
---|---|---|---|
PVA – 3 h | 2.45 ± 0.48 | 1.33 ± 0.17 | 0.64 ± 0.19 |
PVA – 5 h | 2.01 ± 0.09 | 1.05 ± 0.01 | 0.56 ± 0.02 |
PVA – 10 h | 2.02 ± 0.15 | 1.07 ± 0.08 | 0.56 ± 0.08 |
PVA−BTCA – 3 h | 2.05 ± 0.31 | 1.32 ± 0.17 | 0.88 ± 0.48 |
PVA−BTCA – 5 h | 2.34 ± 0.06 | 1.31 ± 0.12 | 0.63 ± 0.00 |
PVA−BTCA – 10 h | 2.23 ± 0.06 | 1.26 ± 0.19 | 0.70 ± 0.15 |
3.6 Adsorption results
In this study, 3, 5 and 10 h collected neat-PVA and PVA− BTCA nanofiber mats and heat was fixated at 130, 150 and 170°C. Then, these nanofibrous mats were evaluated for the color removal of Reactive Red 141. The dye adsorption onto the neat-PVA and PVA−BTCA nanofiber mats was studied as a function of contact time, and the adsorption results are presented in Figure 7.

Amounts of the dye adsorbed versus contact time for PVA and PVA–BTCA nanofibers produced in different collection times and fixation temperatures.
The adsorption capacity (q) increased in time but reached the plateau at the same time (approximately 4–6 h) for different collection times and fixation temperatures. The maximum equilibrium adsorption capacities of the nanofiber membranes after 48 h were equal to 84.36 and 87.40 mg/g for 150°C heat-fixated neat-PVA and PVA−BTCA nanofibers, respectively.
It was observed that there was no significant difference between the neat-PVA and PVA−BTCA nanofiber mats in mean values of adsorption properties. The results of adsorption experiments also showed that collection periods did not significantly affected the adsorbed amount of the dye, they were close to each other. Thus, adsorption capabilities of PVA nanofibers did not rely on the thickness of the PVA mats, and 3 -h collection period was enough for the dye adsorption. However, it was seen that fixation temperature had a significant effect on the dye adsorption. The adsorbed amount of the dye reached the highest and the lowest adsorption rates at 150°C and 130°C, respectively. According to these results, 130°C was not enough and 170°C was too much for the higher adsorption amounts. In all, 150°C of fixation temperature was the most suitable temperature for both the neat-PVA and PVA−BTCA nanofiber mats. These results were also noticeable in the color of the dye solutions after the adsorption process (Figure 8).

Images of the dye baths before and after the adsorption process. *Untreated dye solution (a). The dye solutions after the adsorption with 3 h (b), 5 h (c) and 10 h (d) collected and heat-fixated neat-PVA nanofibers; The dye solutions after the adsorption with 3 h (e), 5 h (f) and 10 h (g) collected and heat-fixated PVA−BTCA nanofibers.
In order to evaluate the morphology of the nanofibers after the adsorption process, SEM images of the nanofibers were taken. In Figure 9, PVA-130 nanofibers were not stable in water; they almost lost their fibrous structure. With the increasing temperature, PVA nanofibers had better preserved their fibrous structure. Although in case of 150°C, PVA-150 nanofiber mats shrunk and nanofibers were entangled. PVA-170 nanofibers were still straight and in a nanofiber form when compared to PVA-150. Adsorption of dye aggregates and particles of Na2SO4 and Na2CO3 could be also seen for both PVA-150 and PVA-170 nanofibers. On the other hand, BTCA crosslinking significantly improved the water stability of the PVA nanofibers when compared to that of heat-fixated neat-PVA nanofibers. Even at 130°C, nanofibers preserved their fibrous structure. In all three cases, adsorption of dye aggregates and particles of Na2SO4 and Na2CO3 could be seen on the surfaces of nanofibers. However, it could be clearly seen from the SEM images that dye aggregates and particles of Na2SO4 and Na2CO3 were also penetrated inside the fibrous structure, so it could be said that preserving the nanofibrous structure has an impact on adsorption of these aggregates and particles.

SEM images of the heat-fixated neat−PVA and PVA−BTCA nanofibers after adsorption studies.
It was clear from the SEM images of the nanofibers after the adsorption process (Figure 9) and weight loss test results (Figure 6) that PVA nanofibers were not stable to water at 130 and 150°C. Thus, to remove the color from the wastewater, PVA nanofibers could be used but PVA nanofibers should be chemically cross-linked properly. According to these results, 150°C heat-fixated PVA–BTCA nanofibers mats are convenient for this application.
The pseudo-first-order kinetic equation (Equation 3) and pseudo-second-order kinetic equation (Equation 5) were also applied to the adsorption data. The parameters of the kinetic models and correlation coefficients are given in Tables 4 and 5. The values of the correlation coefficient implied that the adsorption of the dye on the neat-PVA and PVA−BTCA nanofibers was described by a pseudo-second-order equation.
Parameters of the pseudo-first-order equation
Polymer | Collection time (h) | Fixation temperature (°C) | qe | k1 (s−1) | R2 |
---|---|---|---|---|---|
PVA | 3 | 130° | 76.92 | 91.42 | 0.85 |
150° | 95.24 | 54.67 | 0.73 | ||
170° | 82.65 | 30.59 | 0.47 | ||
5 | 130° | 87.72 | 105.16 | 0.90 | |
150° | 82.65 | 59.17 | 0.73 | ||
170° | 80.65 | 49.26 | 0.69 | ||
10 | 130° | 71.43 | 110.79 | 0.85 | |
150° | 91.74 | 95.40 | 0.89 | ||
170° | 81.97 | 48.03 | 0.68 | ||
PVA–BTCA | 3 | 130° | 87.72 | 103.93 | 0.91 |
150° | 98.04 | 28.63 | 0.44 | ||
170° | 80.00 | 32.06 | 0.49 | ||
5 | 130° | 73.53 | 98.49 | 0.89 | |
150° | 99.00 | 41.15 | 0.61 | ||
170° | 80.65 | 32.00 | 0.49 | ||
10 | 130° | 86.21 | 106.98 | 0.91 | |
150° | 99.00 | 57.32 | 0.75 | ||
170° | 82.65 | 52.24 | 0.71 |
Parameters of the pseudo-second-order equation
Polymer | Collection time (h) | Fixation temperature (°C) | qe (mg·g−1) | k2 (dm3·mol−1·s−1) | R2 |
---|---|---|---|---|---|
PVA | 3 | 130° | 82.65 | 0.00011 | 0.98 |
150° | 87.72 | 0.00028 | 0.99 | ||
170° | 75.76 | 0.00060 | 0.99 | ||
5 | 130° | 86.96 | 0.00012 | 0.99 | |
150° | 86.96 | 0.00014 | 0.99 | ||
170° | 76.92 | 0.00028 | 0.99 | ||
10 | 130° | 86.21 | 0.00007 | 0.96 | |
150° | 87.72 | 0.00014 | 0.99 | ||
170° | 77.52 | 0.00030 | 0.99 | ||
PVA–BTCA | 3 | 130° | 78.13 | 0.00019 | 0.99 |
150° | 87.72 | 0.00070 | 0.99 | ||
170° | 74.63 | 0.00045 | 0.99 | ||
5 | 130° | 76.92 | 0.00012 | 0.98 | |
150° | 90.09 | 0.00037 | 0.99 | ||
170° | 75.19 | 0.00045 | 0.99 | ||
10 | 130° | 79.37 | 0.00016 | 0.99 | |
150° | 90.91 | 0.00025 | 0.99 | ||
170° | 77.52 | 0.00029 | 0.99 |
4 Conclusion
In this study, neat-PVA and PVA−BTCA nanofibers were produced by electrospinning method for the adsorption of Reactive Red 141. TGA was used to evaluate the thermal degradation of the nanofibers versus temperature. TGA results confirm that an increase in thermal stability is a direct consequence of crosslinking with BTCA, and when they were compared with neat-PVA nanofibers, BTCA crosslinking is more effective than heat fixation/self-crosslinking. Mean fiber diameters of the neat-PVA and PVA−BTCA nanofibers were approximately 328.9 and 272.36 nm, respectively, and it was considered to be statistically significant (p < 0.05). The thicknesses of the nanofiber mats significantly affected by the collection period and the thinner PVA−BTCA nanofiber mats were produced due to finer nanofiber diameter. BTCA crosslinking led to a significant decrease in the degree of swelling at 150°C. It was ~650%, and weight loss of the PVA-150 nanofibers was 8%. A slight swelling of the nanofibrous structure occurred with negligible weight loss. According to pore size evaluation, to achieve smaller pore sizes, 3 h of collection with a thickness of 0.029–0.079 mm was enough for ~1 μm MFP. From the adsorption studies, it was seen that the neat-PVA nanofibers could be used for the removal of reactive dye color. However, PVA nanofibers should be chemically cross-linked properly. When the fixation temperatures of 130, 150 and 170°C were compared, 150°C was the most suitable temperature in case of adsorption and water stability results.
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Articles in the same Issue
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- Chemical Hand Warmers in Protective Gloves: Design and Usage
- The Removal of Reactive Red 141 From Wastewater: A Study of Dye Adsorption Capability of Water-Stable Electrospun Polyvinyl Alcohol Nanofibers
- A Review of Contemporary Techniques for Measuring Ergonomic Wear Comfort of Protective and Sport Clothing
- Experimental Study on Dyeing Performance and Antibacterial Activity of Silver Nanoparticle-Immobilized Cotton Woven Fabric
- Sewing Thread Consumption for Chain Stitches of Class 400 using Geometrical and Multilinear Regression Models
- The Status of Textile-Based Dry EEG Electrodes
- Comprehensive Assessment of the Properties of Cotton Single Jersey Knitted Fabrics Produced From Different Lycra States
- Prognosticating the Shade Change after Softener Application using Artificial Neural Networks
- Influence of the Structure of Seersucker Woven Fabrics on their Friction Properties
- Evaluation of Cochlospermum vitifolium Extracts as Natural Dye in Different Natural and Synthetic Textiles
- Homogeneous Coatings of Titanium Dioxide Nanoparticles on Corona-Treated Cotton Fabric for Enhanced Self-Cleaning and Antibacterial Properties
- Numerical Analysis of Large Deflections of a Flat Textile Structure with Variable Bending Rigidity and Verification of Results Using Fem Simulation
- Thermal Behavior of Aerogel-Embedded Nonwovens in Cross Airflow
- Kansei Engineering as a Tool for the Design of Traditional Pattern
Articles in the same Issue
- Photostability of TiO2-Coated Wool Fibers Exposed to Ultraviolet B, Ultraviolet A, and Visible Light Irradiation
- Chemical Hand Warmers in Protective Gloves: Design and Usage
- The Removal of Reactive Red 141 From Wastewater: A Study of Dye Adsorption Capability of Water-Stable Electrospun Polyvinyl Alcohol Nanofibers
- A Review of Contemporary Techniques for Measuring Ergonomic Wear Comfort of Protective and Sport Clothing
- Experimental Study on Dyeing Performance and Antibacterial Activity of Silver Nanoparticle-Immobilized Cotton Woven Fabric
- Sewing Thread Consumption for Chain Stitches of Class 400 using Geometrical and Multilinear Regression Models
- The Status of Textile-Based Dry EEG Electrodes
- Comprehensive Assessment of the Properties of Cotton Single Jersey Knitted Fabrics Produced From Different Lycra States
- Prognosticating the Shade Change after Softener Application using Artificial Neural Networks
- Influence of the Structure of Seersucker Woven Fabrics on their Friction Properties
- Evaluation of Cochlospermum vitifolium Extracts as Natural Dye in Different Natural and Synthetic Textiles
- Homogeneous Coatings of Titanium Dioxide Nanoparticles on Corona-Treated Cotton Fabric for Enhanced Self-Cleaning and Antibacterial Properties
- Numerical Analysis of Large Deflections of a Flat Textile Structure with Variable Bending Rigidity and Verification of Results Using Fem Simulation
- Thermal Behavior of Aerogel-Embedded Nonwovens in Cross Airflow
- Kansei Engineering as a Tool for the Design of Traditional Pattern