Document Type : Research Paper
Authors
Department of Chemistry, Faculty of Science, Golestan University, Gorgan, Iran
Abstract
Keywords
INTRODUCTION
Organic dyes containing azo group and aromatic rings are very toxic, stable, non-biodegradable, and carcinogenic. They were used as colorants in various industries such as leather, food, paper, and textile [1]. The discharge of industrial wastewater into the nearby water source causes the pollution of aquatic systems [2], which may lead to cancers, tumors, allergies, and mutations in humans [3]. Thus, the industrial wastewater should be treated before its discharge into the environment using different techniques [4-8]. Among them, the adsorption process is one of the most important techniques for the removal of organic dyes using various compounds as adsorbents due to being simple, low cost, highly efficient, and without second pollution [9-12].
Eosin Y (EY) as anionic dye (Scheme 1) is a pink colored which exhibits yellow green fluorescence and is widely used in the Gram straining of the bacterial strain [13]. In addition, eosin Y is used in dying, printing, and paints factory [14]. However, it causes damages to liver, lungs, eyes, skin, and kidneys [13]. Until now, various techniques have been available for the removal of eosin Y dye from aqueous solutions [15-17]. However, removing organic dyes using adsorption process has been widely used due to its low cost, simplicity and high efficiency [18-20]. Various solid materials are used as adsorbent for the removal of organic dyes such as transition metal oxide nanoparticles [21,22] as well as their polymeric nanocomposites [23-25]. In recent years, the adsorption process was performed to remove different organic dyes by modifying various polymers such as PVA [26], modified chitosan [27-29], and PVP [30-32].
Poly(vinyl pyrrolidone) (PVP) is a water-soluble synthetic homopolymer; it is also neutral, biodegradable, low cost, non-toxic, hydrophilic, and biocompatible, which has numerous potential applications [33-39] such as the delivery of drugs [40], removal of organic dyes [30-32], and pharmaceutical formulations [41]. Moreover, polyvinylpyrrolidone (PVP) can be extensively used in order to prevent particle aggregation and control the average particle size and shape of nanoparticles [42]. The incorporation of transition metal oxide into a PVP matrix can improve the chemical and physical properties [33-39, 43].
In the present paper, we synthesized PVP/NiO nanocomposite via the co-precipitation technique and characterized. In addition, the adsorption study was examined for the removal of eosin Y (EY) dye from aqueous solution.
EXPERIMENTAL
All reagents, such as polyvinyl pyrrolidone (PVP) and eosin Y, were purchased from Merck Co. NiO nanoparticles were prepared according to the previous literature [27]. FT-IR spectrum of PVP/NiO was recorded by spectrophotometer instrument (Perkin-Elmer) (KBr disks, 4000–400 cm-1). X-ray diffractometer (2θ = 10-80º, Bruker AXS-D8) was applied to determine XRD pattern. DSC analysis was recorded by a DSC analyzer (Model 60A, Shimadzu, Japan). FE-SEM images were recorded on the TESCAN Vega Model scanning electron microscope. UV-Vis spectra were carried out with a UV-Visible spectrophotometer (Perkin-Elmer).
1 g of PVP was suspended in 10 mL of ethanol and stirred for 10 min. Then, 0.25 g of NiO nanoparticles was added and magnetically stirred for 6 h. After the evaporation of the solvent, the gray precipitates were washed twice with distilled water, then dried at room temperature and characterized.
The EY dye adsorption capacity was evaluated by placing 0.012 and 0.025 g of PVP/NiO in 70 mL of a 20 mg/L EY dye aqueous solution at room temperature. The pH of the EY solutions was adjusted using 0.1 M NaOH or 0.1 M HCl until the desired pH (2–11) was obtained. At predetermined time intervals (0-90 min), 3 mL of the solutions were sampled to evaluate the EY content residual in the solution by UV-vis spectroscopy. The dye content in the supernatant solution was obtained by measuring the sample’s absorptivity. The analyses of EY dye adsorption capacities were conducted using the following equation:
where, R is the removal percentage and qt is the amount of EY dye adsorbed at different contact time; Ci represents the initial concentration of EY dye (mg/L); Ct denotes EY concentration at different contact time (mg/L); V is the volume of the EY dye solution (L), and M is the mass of PVP/NiO (g).
RESULTS AND DISCUSSION
FT-IR
The FT-IR spectra of PVP and PVP/NiO nanocomposite are presented in Fig. 1. PVP and PVP/NiO demonstrate a broad peak at about 3450 cm-1 assigned to O-H band and also adsorbed water molecules [44-47]. Additionally, a peak at 1675 cm-1 is assigned to the C=O absorption bands [33-39]. The peaks at about 2950 cm-1 are ascribed to the symmetric CH2 stretching [33-39], while the band at about 1440 cm-1 is attributed to the CH2 bending [33-39]. A sharp peak at 441 cm-1 in PVP/NiO is assigned to the Ni-O stretching mode [44-47].
XRD
The XRD patterns of PVP and PVP/NiO nanocomposite are shown in Fig. 2. PVP shows two broad peaks at 11 and 20° and these peaks are observed in PVP/NiO at 2θ of 11.5 and 21°. The intensity of the peaks in PVP/NiO is lower than that of similar peaks in pure PVP and NiO nanoparticles, indicating a decrease in the crystallinity of the synthesized PVP/NiO compound [44-47]. In addition, in the XRD pattern of NiO/PVP, there are five sharp and narrow peaks at 2θ of 37.3, 43.4 63.1, 75.6 and 79.5°, corresponding to (111), (200), (220), (311) and (222) crystal planes of cubic NiO (JCPDS card no. 47-1049) [44-47], confirming the successful preparation of PVP/NiO nanocomposite.
TGA-DSC
TGA and DSC curves of PVP and PVP/NiO nanocomposite are presented in Fig. 3. PVP and PVP/NiO show a mass loss of ≈ 7% and ≈ 3%, respectively, in the first stage at about 100 °C, assigned to the removal of moisture and water molecules adsorbed. Their mass losses at temperatures up to ≈ 365 °C for PVP/NiO and 410 °C for PVP are almost negligible. After that and up to 450 °C, PVP and PVP/NiO nanocomposite show a mass loss of 91% and 52%, respectively. Finally, at 800 °C, the remaining mass of PVP and PVP/NiO is ≈ 0% and ≈ 45%, respectively. The mass loss of PVP and PVP/NiO can be explained in more detail by DSC thermogram (Fig. 3b). A mass loss process observed at 105 and 80 °C for PVP and PVP/NiO, which indicates the evaporation of moister or water molecules. A sharp peak related to the main decomposition stage of PVP and PVP/NiO was seen at 453 and 435 °C, respectively [39,43].
SEM-EDS
SEM images of PVO and PVP/NiO nanocomposite are presented in Fig. 4. PVP has an almost smooth surface with varying particle sizes and also particles are stacked on top of each other. By adding NiO nanoparticles to PVP, many number of pores have been created between the PVP particles, which enhances the interaction between the EY molecules with PVP/NiO and can provide a large number of active adsorption sites. The NiO nanoparticles are spherical in shape, with a particle size ranging from 40-70 nm.
EDS spectra of PVP and PVP/NiO nanocomposite are shown in Fig. 5. It can be seen that the contents of C and H of PVP simultaneously decreased, while the O and Ni contents increased, indicating the successful deposition of NiO onto the PVP polymer and preparation of PVP/NiO nanocomposite.
Adsorption study of eosin Y (EY)
The adsorption of eosin Y (EY) was investigated by UV-Vis spectrophotometer in order to measure the absorbance intensity in 520 nm using PVP/NiO. Fig. 6 illustrates the maximum absorbance of EY solution after different contact time at the presence of various doses of PVP/NiO, and shows the decrease of absorbance intensity by increasing contact time, confirming that the removal of EY from aqueous solution by PVP/NiO nanocomposite.
In the removal of different organic dyes from the aqueous solution, the solution pH plays an important role in the adsorption process due to controlling the surface charge of adsorbent [20]. In this paper, the effect of pH on the removal efficiency of EY using PVP/NiO was studied in the pH range of 3-5 as shown in Fig. 7. It is seen that the removal efficiency of EY decreases with increasing pH [1,2,48], and about 99.98% removal is obtained at pH 3 in the presence of 0.025 f of PVP/NiO.
Due to the protonation of the active sites on the surface of PVP/NiO at low pH, which enhances the electrostatic attraction between the PVP/NiO surface and anionic EY molecules, the removal percentage was increased [1, 2, 48]. By increasing the pH solution, the active groups of PVP/NiO underwent deprotonation due to the decrease of H+ ions. At the pH solution of 5, the removal percentage of EY molecule dye was found to be very low (<10%). Then, the pH solution of 3 was selected for the investigation of contact time and adsorbent dose.
The effect of PVP/NiO dose (0.012 and 0.025 g) and contact time (0 – 90 min) on the removal of EY is illustrated in Fig. 8. It can be seen that the removal percentage of EY was increased with increasing PVP/NiO due to the increase of the active sites on the surface of the sorbent as well increased contact time [1,2,48]. At optimal condition, the maximum removal percentage of EY dye reached 99.98% (Fig. 8). The maximum adsorption capacity was found to be 101.58 mg/g using 0.012 g of PVP/NiO (Fig. 8).
Kinetic studies
The adsorption kinetic of the removal of EY dye was studied by the first and second order models using the following equations (Figs. 9 and 10) [24,49].
log(qe-qt) = loqqe – (k1/2.303)t (3)
(t/qt) = (1/k2qe2) + t/qe (4)
Where, k1 and k2 are the rate constants for first and second order kinetic models; qe and qt are EY concentration at equilibrium and particular time, respectively. As seen in Fig. 8, the kinetic linear curves showed that the adsorption of EY dye follow a pseudo second-order model [1,50].
Adsorption mechanism
Previous studies on the removal of different colors with the help of polymer composites have demonstrated that color removal is done by various interactions such as H-bonding, π-π interaction, n-π interaction, and electrostatic attraction [27-29]. According to the adsorption results of EY removal and functional groups on the surface of PVP/NiO composite, the main cause of EY dye removal is n-π interaction, which is shown in Scheme 2. This interaction occurs between the lone-pairs of O and N electron-donation on the surface of PVP/NiO and the aromatic rings of the EY molecules.
CONCLUSIONS
In this study, new PVP/NiO nanocomposite was synthesized, characterized and used as a new sorbent for the removal of eosin Y from aqueous solution. The results demonstrated that the maximum adsorption capacity was found to be 101.58 mg/g at pH solution of 3, using 0.0125 g of sorbent after 90 min contact time. These results reveal that the PVP/NiO could efficiently remove EY dyes. The kinetic studies showed that the adsorption of EY dyes follow a pseudo second-order model, which involves n-π interaction. Thus, PVP/NiO nanocomposite could be studied as a new potential sustainable candidate for the removal of other harmful organic dyes.
ACKNOWLEDGMENTS
The authors are grateful to Golestan University for supporting this research.
CONFLICT OF INTEREST
The authors declare no conflicts of interest.