The different processing stages involved in the synthesis of Ag-doped titania coated chitosan beads are presented below in Fig. 2. The color of the chitosan wet gel beads was found to change from white to brown after coating with Ag-doped titanium dioxide and freeze-drying for 1 hour. Pure chitosan beads after freeze-drying have shown less mechanical stability whereas the freeze-dried/oven-dried chitosan beads with Ag-doped titania coating have exhibited sufficient mechanical stability for handling. Silver doped titanium dioxide was characterized for its structural, textural, and morphological features and the results are presented below.
XRD analysis of undoped and Ag-doped titanium dioxide is presented in Fig. 3. XRD analysis of the Ag-doped TiO2 shows the presence of phase pure anatase (JCPDS Card No: 00-021-1272) which is reported to be highly beneficial for the photocatalytic reduction of nitrate (Reyes-Coronado et al. 2008). No peaks corresponding to silver species were observed indicating that the addition is well below the doping level (below 2%) which is too low to show clear peaks.
Five minutes of microwave treatment of the synthesized titania sol (Peiró et al. 2001) and the silver doped titania sol has resulted in the crystallization of titanium dioxide in the anatase phase. Microwave heating of aqueous titania sol is reported to enhance the crystallization of titania as the presence of water as a solvent favors the crystallite formation (Smitha et al. 2013). Microwave energy is easily absorbed by polar solvents such as water resulting in homogeneous nucleation of the system due to the rapid energy transfer involved during the treatment. Kinetics of the crystallization of titania sol is significantly improved via the use of microwaves for a shorter duration (Dufour et al. 2012). Moreover, microwave energy facilitated the predominant growth of anatase crystallites suitable for photocatalytic application.
Figure 4 represents the morphological analysis of undoped titania and Ag-doped titania, microwave treated for five minutes. Nanosized titania particles are visible from the SEM images. The average particle size of titania was ~ 5–6 nm for undoped titania whereas it was ~ 3–4 nm for the 0.5 mol% Ag-doped titanium dioxide. TEM analysis of the TA-0.5 sample also shows the presence of anatase TiO2 with a particle size as small as 3–4 nm. Particle sizes obtained from the SEM/TEM analysis were consistent with the crystallite sizes calculated from the XRD analysis for the anatase crystals using the Debye Sherrer Equation as the values were 5.4 nm and 4.8 nm for the undoped titania and Ag-doped titania (TA-0.5) respectively.
Reduction in the particle size of titanium dioxide to Ag doping is already reported in the literature which is ascribed to the decrease in the particle nucleation during hydrolysis/condensation of Ti(IV)isopropoxide in presence of silver species (Mogal et al. 2014). According to the researchers, there exists a critical Ag concentration above which the particle size increases (Li et al. 2020). Figure 5 presents the N2 adsorption-desorption isotherms and the pore size distribution of the pure titania and the silver doped titania. A type IV isotherm with a hysteresis loop characteristic of the mesoporous materials was obtained from the surface area analysis (Sotomayor et al. 2018). Pure titania had a surface area of 251 m2g− 1 (Table I). Among the different samples, TA-0.5 has shown the highest surface area of 282 m2g− 1. There was only a marginal increase in the surface area for the 1 mol% Ag-doped sample when compared to the undoped sample and it was found to decrease further by increasing the percentage doping. The fine mesoporous structure of the titanium dioxide and Ag-doped titanium dioxide as evident from a monomodal pore size distribution is also very clear in Fig. 5b. TA-0.5 has shown a narrow pore size distribution when compared to that of other samples.
Table I. Textural features of titania and Ag doped titania, microwave treated for 5 minutes.
Sample | BET Surface Area (m2g− 1) | Total Pore Volume (cm3g− 1) | Micropore Volume (cm3g− 1) | Mesopore Volume (cm3g− 1) | Pore diameter (nm) |
TA-0 | 251.4 | 0.3043 | -0.0195 | 0.3238 | 4.8 |
TA-0.5 | 282.3 | 0.3150 | -0.0131 | 0.3281 | 4.5 |
TA-1 | 253.6 | 0.2904 | -0.0178 | 0.3082 | 4.6 |
TA-2 | 227.8 | 0.3343 | -0.0123 | 0.3466 | 4.7 |
The high surface area of the TA-0.5 sample obtained here could be due to the reduction in the crystallite size due to the effective doping by the Ag ions. The Ag ions existing on the surface of anatase titania particles can hinder the mutual contact and material transfer between the anatase grains, thereby depressing the grain growth of anatase leading to an increased surface area (Chao et al. 2003).
The UV-Visible absorbance of pure titanium dioxide and TA-0.5 was further recorded using a UV-Visible spectrophotometer and the obtained results are presented in Fig. S5. Absorption in the visible region (400–800 nm) was more for Ag-doped titania when compared to that of pure titania indicating that Ag-doped TiO2 may be active under visible light irradiation (Li et al. 2011).
Figure 6 represents the FTIR analysis of the undoped titania coated chitosan beads and the 2 mol% Ag-doped titania coated chitosan beads. FTIR spectra mainly show the vibrational modes of chitosan in the undoped and Ag-doped systems (de Souza et al. 2015). The broad band centered at 3300 cm− 1 shows the overlapping of O-H and N-H stretching vibration, together with N-H secondary amine stretching of the cross-linked chitosan. The presence of bands corresponding to amides was noted at 1633 cm− 1 and 1550 cm− 1. The band at 1026 cm− 1 and 1072 cm− 1 is attributed to the C–O stretching vibration contributed by the primary alcohol in chitosan. Bands corresponding to CH2 bending and C-O-C asymmetric stretching vibration were also observed at 1411 and 1155 cm− 1 respectively. Ag-doped TiO2-coated chitosan beads contain a trace amount of silver oxide in them. The different peaks obtained from the FTIR spectra are assigned to their respective vibrational modes as given in Table II.
Both the samples had characteristic Ti-O-Ti stretching vibration for TiO2 at 410 cm− 1 (Vasconcelos et al. 2011) whereas TA-2 coated chitosan beads contain a small peak at 455 cm− 1 corresponding to the presence of oxidized silver species (Ag2O) (Pawar et al. 2016).
Table II. FTIR peak assignment (de Souza et al. 2015) for TA-0 and TA-2 coated chitosan beads, freeze-dried for 1 hour.
No. | FTIR peak (cm− 1) | Vibrational Mode | Assignment |
a | 3220–3380 | NH & OH Stretching | Amines & H2O |
b | 1633 | N-H bending vibration | Secondary amide |
c | 1550 | N-H bending vibration | Secondary amide |
d | 1411 | CH2 bending | Pyranose ring |
e | 1155 | C-O-C asymmetric stretching | from β(1–4) bond |
f | 1072 | C-O stretching | Primary OH |
g | 1026 | C-O stretching | Primary OH |
h | 410 cm− 1 | (Ti-O-Ti) stretching vibration | TiO2 |
Other vibrational peaks obtained for NH, OH, CH2, CO, etc. are characteristic of the chitosan polymer which is present in both the samples. Thus, FTIR analysis revealed the successful formation of the chitosan-titania nanocomposite as evidenced by the characteristic peaks corresponding to the chitosan and titanium dioxide.
SEM analysis of the pure chitosan beads and the 0.5 mol% Ag doped titania coated chitosan beads, after freeze-drying for 1 hour is presented in Fig. 7.
The microporous structure of the prepared chitosan beads is very clear from the SEM images with an average pores size of ~ 0.5 mm. Ag-doped TiO2 gets coated uniformly over the porous surface of chitosan which eventually decreases the pores size of chitosan (Jayakumar et al. 2011) from ~ 0.5 mm to ~ 0.25 mm. TA-0.5 coated chitosan beads have shown hard agglomerates on the surface of the beads could be due to the presence of excess TiO2 that gets precipitated out.
The photocatalytic reduction of nitrates by the freeze dried nanocomposite beads was monitored by measuring the concentration of nitrate ions in the model water sample (spiked with nitrate ions) subjected to photocatalytic studies under sunlight for 2 hours in the presence of a hole scavenger. Undoped titania and Ag-doped titania coated chitosan beads were subjected to a photocatalytic reduction study. The nitrate solution along with the coated chitosan beads was kept in the dark for about half an hour to nullify the effect of any adsorption by the porous structured chitosan beads. Table III provides the adsorption and photocatalytic efficiency of the synthesized chitosan beads with varying Ag concentrations towards nitrate anion. The obtained results clearly shows that Ag doping on titania is affecting the adsorption characteristics of the synthesized chitosan beads. The sample, CTA-0.5, the one containing 0.5 mol% Ag-doped titania coated chitosan beads are showing a nitrate adsorption efficiency of 43.5%. The smaller particle size (~ 10 nm) and enhanced surface area of the TA-0.5 sample might have contributed to the relatively high adsorption efficiency (Tian et al. 2008). About 95% nitrate reduction efficiency was observed for the sample CTA-0.5 which was the highest efficiency among the other samples. Undoped titania-coated chitosan beads had a nitrate reduction efficiency of 42%.
Table III. Adsorption efficiency of the undoped and Ag-doped titania coated chitosan beads towards nitrates.
Sample | Initial nitrate concentration (ppm) | Remaining nitrate after adsorption (ppm) | Adsorption efficiency (%) | Photocatalytic efficiency (%) |
CTA-0 | 166 | 100.9 | 39.2 | 42 |
CTA-0.5 | 166 | 93.7 | 43.5 | 95 |
CTA-1 | 166 | 100.7 | 39.3 | 37 |
CTA-2 | 166 | 93.4 | 43.7 | 80 |
According to the researchers, many factors such as particle size of titanium dioxide, reaction temperature, the metal used for doping, and hole scavenger and its concentration can influence the photocatalytic nitrate reduction efficiency. The hole scavenger formic acid used in the study aids in achieving significantly higher nitrate conversion (Doudrick et al. 2013). A decrease in the particle size of titanium dioxide due to the Ag doping in the present work increases the amount of exposed unit area per unit mass which increases the adsorption efficiency. The metal species (Ag) clusters incorporated on the TiO2 surface can induce the formation of oxygen vacancies which act as electron traps (Pan et al. 2013). The new allowed electronic states below the TiO2 conduction band enhance the visible light absorption of the photocatalysts which makes them active even under sunlight due to the band gap energy modification. Moreover, the new energy levels created can act as an electron sink, which improves the electron-hole separation and thus more electrons will be available on the catalyst surface for the nitrate reduction reaction (Sa et al. 2009). The UV-visible absorbance spectra of pure TiO2, Ag doped TiO2 and the mechanism behind the photocatalytic nitrate reduction (Kobwittaya and Sirivithayapakorn 2014) is presented in Fig. 8.
It is assumed that the end product of the nitrate reduction reaction in the present work is N2 as no nitrites were measured during the ion chromatographic (IC) analysis of the samples collected and there was no significant change in the pH of the sample out of NH4+ ions. Thus, in the present work, Ag-doped TiO2 coated chitosan beads (CTA-0.5) show superior nitrate reduction efficiency and adsorption efficiency which makes it a suitable candidate for the removal of nitrates from water/wastewater. The nanocomposite CTA-0.5 was selected for further studies considering its high adsorption as well as photocatalytic efficiency towards the removal of nitrate from water.
Figure 9 represents the surface morphology of oven-dried pure chitosan beads and Ag-doped TiO2 coated chitosan (CTA-0.5) beads. The porous structure of the chitosan bead was considerably changed for the oven-dried sample when compared to that of the freeze-dried sample. The pore size of the pure chitosan beads was in the range of 50–100 nm whereas the mesoporous structure of the chitosan beads was uniformly covered with nanoparticles of titanium dioxide with a size less than 10 nm as revealed from Fig. 9b-c.
Batch/column adsorption cum photocatalytic experiments were also carried out using the CTA-0.5 nanocomposite beads in its oven dried form as it exhibits more mechanical stability when compared to the freeze dried sample. Results on the nitrate adsorption study of pure chitosan beads and CTA-0.5 beads (oven dried) under dark conditions are presented below in Fig. 10a. From the results, it is clear that Ag-doped TiO2 coating over the chitosan beads significantly increases the adsorption efficiency of the beads, and the adsorption of nitrates is getting saturated within 1 hour of stirring under dark conditions as major concentration changes of nitrates was not observed further. Figure 10b demonstrates the adsorption cum photocatalytic efficiency of the oven dried chitosan beads coated with Ag-doped TiO2 in removing nitrates from model contaminated water.
The adsorption efficiencies were 10.9% and 54–60% for the pure chitosan beads and Ag-doped TiO2 coated chitosan beads respectively under dark stirring conditions for 1 hour. The photocatalytic efficiencies were ~ 8.8% for pure chitosan beads whereas it was 70%, 69% and 53% for Ag-doped TiO2 coated chitosan beads with nitrate: formate ratio 1:2, 1:5 and 1:8 respectively in 2 hours of UV irradiation time. Pure chitosan beads lack photocatalytic activity while an enhanced photocatalytic efficiency of the nanocomposite system was observed in the presence of formic acid scavenger.
When the nanocomposite is irradiated with incident light having energy greater than the band gap of titanium dioxide, electrons and holes are generated that can be utilized for the reduction and oxidation, respectively. However, the recombination of the electron and holes in a few nanoseconds can slow down the redox reactions on the surface of the semiconductor and hence adding a hole scavenger (i.e., electron donor) can help overcome the recombination effect and provide a continuous supply of electrons for the nitrate reduction reaction. Formic acid scavenger is reported to have highest activity among other scavengers and the overall redox reaction between nitrate and formic acid with TiO2 under UV irradiation could be represented as given below when the formate: nitrate ratio is 1:2.5 (Yang et al. 2013).
2NO3−+5HCOOH + 2H+→N2 + 5CO2 + 6H2O (5)
During nitrate reduction reaction, both formic acid and nitrate will get consumed and an ideal stoichiometric ratio of 2.5 between the formate and nitrate is considered to offer 100% N2 selectivity. The photocatalytic efficiencies were nearly same when the nitrate:formate ratio was 1:2 to 1:5 in the present study and the formic acid scavenger helps in attaining significantly higher nitrate conversion as it can abstract the holes thereby making more electrons available for the nitrate reduction reaction.
Figure 11 demonstrates the results on the continuous flow adsorption cum photocatalytic studies of the nanocomposite beads carried out in an experimental set up fabricated in-house. Figure 11a shows the effect of the integrated adsorbent-cum photocatalyst system in reducing the nitrate levels well below the permissible limits of standard drinking water in a fixed bed continuous flow system even up to 5 hours whereas the nitrate levels increase above the permissible limits in 200 min itself if we are exploring only the adsorption property of the material. Figure 11b-c shows that as the bed height of the column increases from 6 to 12 cm, there is a prominent effect on the nitrate removal characteristics and nitrate removal for a longer time can be enabled by increasing the bed height to a desired level. The nitrate removal percentage is increased from 49.6–60.8% and to 97.5% when the bed height is increased from 6 cm, 8 cm and to 12 cm in 5 hours time. A larger amount of nitrate gets adsorbed when the bed height is high due to an increase in the surface area of adsorbent cum photocatlyst, providing more binding sites for the adsorption, followed by photocatalytic removal.
The effect of concentration was also studied using continuous flow adsorption cum photocatalysis study in the fabricated water treatment set up that shows a nitrate removal efficiency of 87.6% & adsorption capacity 7.9 mgg− 1 for 8 hours when using an inlet concentration of 100 ppm for a bed height of 12 cm at 5.0 mlmin− 1 flow rate. The nitrate removal efficiency was 55.5% with an adsorption capacity of 7.3 mgg− 1 for 5 hours when using an inlet concentration of 250 ppm for a bed height of 12 cm at 5.0 ml/min flow rate.
In summary, the variations in the residual nitrate are prominent when the amount of catalyst is low and at higher initial concentration of nitrate, and at high flow rate conditions, indicating the need for scavenger addition at a minimum level for a higher overall nitrate removal efficiency in the continuous flow system of adsorption cum photocatalysis. Considering the relatively high adsorption efficiency of the synthesized functional nanocomposite beads, a column adsorption alone experiment was also performed and the results obtained for the adsorption of various anions from a real groundwater sample are presented below in Table IV.
Table IV: Results of the column adsorption study using functional nanocomposite beads.
Sample | Anions | Initial concentration (ppm) | Concentration after adsorption for 20 min (ppm) | Adsorption efficiency (%) |
Pure chitosan bead- | Nitrate | 31.4 | 15.4 | 50.8 |
CTA-0.5 bead | Nitrate | 31.4 | 4.4 | 85.9 |
Pure chitosan bead | Sulphate | 29.0 | 27.0 | 6.9 |
CTA-0.5 bead | Sulphate | 29.0 | 1.0 | 96.5 |
Pure chitosan bead | Phosphate | 0.84 | 2.9 | --- |
CTA-0.5 bead | Phosphate | 0.84 | 0.81 | 3.6 |
Pure chitosan bead | Chloride | 127.9 | 121.9 | 4.7 |
CTA-0.5 bead | Chloride | 127.9 | 51.9 | 59.4 |
It was found that the synthesized functional nanocomposite beads are highly efficient in the removal of nitrates and other anions present in a real groundwater sample when compared to that pure chitosan beads. The mechanism behind the removal of nitrates and other anions is attributed to the electrostatic attraction by the positively charged TiO2 coated chitosan beads. Thus, the efficiency of the functional nanomaterial synthesized in the present work for the removal of multiple ions from groundwater samples suggests the potential of the material for water/wastewater filtration application.