3.1. Analyzing the characterization results
3.1.1. XRD, BET, and UV-Vis characterization
XRD was used for examining the three catalysts, TiO2, Nd-TiO2, and MIP-Nd-TiO2, for phase detection. Figure 2(a) illustrates the 2θ values of 25.32°, 37.79°, 48.14°, 54.09°, 62.82°, and 75.12° matched to the diffraction peaks of anatase TiO2 according to the standard diffraction card (PDF# 21-1272), indicating that materials exhibited pure anatase phase, which facilitates the absorption of light with higher photocatalytic catalytic activity. The XRD patterns did not exhibit any distinct peaks associated with Nd2O3. The reason for this is that when Nd3+ ions penetrate the TiO2 crystals, the amount of Nd2O3 is very small and highly dispersed in TiO2. Nd3+ may be seen either as an amorphous phase that is adsorbed onto the outside of TiO2 or as an inclusion inside the TiO2 lattice(Marcì et al 2001).
All three materials were investigated using the BET test, and the findings are presented in Fig. 2(b). The N2 adsorption-desorption isotherms of the three catalysts exhibit Type IV isotherms with H3-type hysteresis behavior, based on the IUPAC. This behavior is characteristic of mesoporous materials.(Liu et al 2023). The majority of the pore size distributions of the three materials illustrated in Fig. 2(c) range between 0 and 20 nm and the preparation of catalysts with mesoporous characteristics was confirmed by this result. TiO2, Nd-TiO2, and MIP-Nd- TiO2 had specific surface areas of 12.02 m2/g, 65.90 m2/g, and 86.85 m2/g, correspondingly, as displayed in Table 1. As contrasted to TiO2 and Nd-TiO2, the specific surface area of MIP-Nd-TiO2 rose dramatically, and the reaction sites were increased due to the larger specific surface area, which led to the improvement of photocatalytic performance.
The UV-visible spectroscopy technique was used to investigate the optical absorption characteristics of the synthesized materials. The optical absorption edge thresholds of TiO2, Nd-TiO2, and MIP-Nd- TiO2 are illustrated in Fig. 2(d), where they are 434 nm, 431 nm, and 430 nm, respectively. Using the empirical equation Eg = 1240/λ(Qi and Wang 2020), the prohibited band widths of the three catalysts were determined to be 2.85 eV, 2.88 eV, and 2.89 eV, correspondingly. In contrast to TiO2 and Nd-TiO2, the optical absorption edge of MIP-Nd-TiO2 shows a very little degree of blueshift, but exhibits an upward shift in the wavelength range of 450–800 nm, indicating an improvement in visible light absorption. This increase in absorption may be attributed to Nd elemental doping and the incorporation of imprinted molecules.
Table 1
Specific surface area (SBET), pore volume (Vp), and average pore size (Dp) of the different catalysts
Catalyst | SBET(m2/g) | Vp(cm3/g) | Dp(nm) |
TiO2 | 12.02 | 0.06 | 2.82 |
Nd-TiO2 | 65.90 | 0.12 | 7.31 |
MIP-Nd-TiO2 | 86.85 | 0.14 | 6.21 |
3.1.2. TEM characterization
To further analyze the surface morphology and microstructure of the synthesized materials, TEM characterization of the samples was carried out. Figure 3(a), (b), and (c) illustrate 100 nm TEM images of the synthesized material. We can observe that the agglomeration phenomenon of pure TiO2 is more serious, and the agglomeration phenomenon of MIP-Nd-TiO2 has not been so obvious compared to that of TiO2 and Nd-TiO2 with a greater improvement. MIP-Nd-TiO2 has a smaller particle size, and the particle distribution can be more clearly observed, indicating that doping Nd elements and adding imprinted molecules can effectively reduce the inter-particle aggregation, which may enable it to have a larger specific surface area, and this aligns with the findings shown in Table 1. The introduction of Nd elements and imprinted molecules during the synthesis of modified TiO2 samples did not significantly change the overall morphology of the catalysts can be observed. Figure 3(d) displays a 5 nm TEM image of MIP-Nd-TiO2, where a lattice stripe of 0.352 nm can be clearly observed, corresponding to the (101) crystal plane of anatase, which conforms to the XRD characterization results (Fig. 2(a)). In summary, the agglomeration of MIP-Nd-TiO2 particles was suppressed and the particle size was small, so there were more photocatalytic active sites with higher photocatalytic activity.
3.1.3. XPS characterization
XPS was used to investigate the valence states of the elements in MIP-Nd-TiO2. The XPS spectra of O, Nd, C, and Ti elements were detected, corresponding to O 1s, Nd 3d, C 1s, and Ti 2p, as depicted in Fig. 4(a). The Ti 2p XPS spectra of MIP-Nd-TiO2 are displayed in Fig. 4(b). The electronic orbitals of Ti 2p3/2 and Ti 2p1/2 are represented by these peaks, which are situated at 458.45 eV and 464.15 eV of the binding energy. Suggests that the presence of TI is in the form of Ti4 + in MIP-Nd-TiO2(Luo et al 2017). Figure 4(c) displays the O 1s XPS spectra of MIP-Nd-TiO2. Lattice oxygen in TiO2 contributes to the material's peak at 529.72 eV, whereas the presence of hydroxyl groups (-OH) results in a peak at 532.05 eV (Qin et al 2024). The Nd 3d XPS spectra of MIP-Nd-TiO2 are illustrated in Fig. 4(d), where two prominent peaks matching the Nd 3d5/2 and Nd 3d3/2 orbitals are located at 974.43 eV and 994.19 eV, respectively, indicating that the sample doped Nd exists in the form of Nd3+ (Nithya et al 2018). Overall, the XPS characterization results showed proof of successful doping of Nd, proving that the MIP-Nd-TiO2 catalyst was successfully synthesized.
3.1.4. FT-IR and PL characterization
FT-IR spectroscopy was used to examine the materials' functional groups. All three catalysts exhibited -OH peaks at 1324 cm− 1 and 3327 cm− 1, as illustrated in Fig. 5(a), as a result of the absorption of CO2 and O2 from the surrounding air. Among them, Nd doping and the addition of imprinted molecules resulted in larger peaks due to increased ligand bonding and the creation of new bonds, respectively. The O-H stretching vibration peaks of carboxylic acid dimers are 2850 cm− 1 and 2779 cm− 1(Zhu et al 2020), where the MIP-Nd-TiO2 produced new peaks at 2349 cm− 1, and the strong hydrogen bonding formed may increase its performance in degrading pollutants. It can be clearly observed that no functional groups such as lipid and amide bonds were found for MIP-Nd-TiO2 at 1680 cm− 1-1750 cm− 1, indicating that the imprinted molecules were completely eluted.
Figure 5(b) shows the PL patterns of the three species of catalysts, the PL peaks of MIP-Nd-TiO2 are conspicuously diminished in comparison to those of Nd-TiO2 and TiO2. A decrease in the intensity of the PL peaks of the catalysts corresponds to a reduction in the rate of electron-hole pair complexation. This indicates that the charge transfer effect is enhanced and electron-hole pair recombination is impeded(Ma et al 2024). This phenomenon improves the photocatalytic performance. The lowest spectral peak of MIP-Nd-TiO2 among the three catalysts represents the better photocatalytic performance of MIP-Nd-TiO2.
3.2. Catalyst degradation performance studies
3.2.1. Influence of catalyst doping ratio on catalyst degradation performance
To achieve the most efficient degradation of OTC by the catalyst, the optimal Nd and Ti doping ratios as well as the optimal doping content for molecular imprinting were explored, and the orthogonal experimental bubble diagrams with different Nd doping ratios and OTC doping are shown in Fig. 6(a). The results of the preexisting experiments show that there is almost no enhancement for n(Nd)/n(Ti) < 1% and m(OTC) < 0.1 g. The poor enhancement effect may be due to the small hindering effect on photogenerated carrier complexation or incomplete formation of imprinted cavities when the doping amount of Nd or molecular imprinting is too small. It is evident from Fig. 6(a) that the bubble volume is highest when n(Nd):n(Ti) = 1.25:100 and m(OTC) = 0.15 g. The highest OTC degradation rate of the synthesized catalyst under these conditions reaches 91.97%, which is a 1.42-fold enhancement compared to that of the pure TiO2 without any doping, which is 64.34%, for the degradation rate of OTC. It indicates molecular imprinting adding and Nd doping enhanced the photocatalytic capacity of TiO2.
3.2.2. Influence of variation of calcination temperatures on the degradation performance of catalysts
Figure 6(b) illustrates the impact of MIP-Nd-TiO2 on OTC degradation at calcination temperatures of 450, 500, and 550 ℃. As the calcination temperature was raised from 450 ℃ to 500 ℃, the degradation performance of MIP-Nd-TiO2 increased; As the calcination temperature was raised from 500°C to 550°C, the degradation performance of MIP-Nd-TiO2 reduced. At 500°C, the MIP-Nd-TiO2 degrading performance was the best, which indicated that the TiO2 calcined at 500 ℃ was in the phase of pure anatase, and the photocatalytic effect of MIP-Nd-TiO2 was the best at this time.
3.2.3. Influence of variation of calcination time on the degradation performance of catalysts
The degrading impact of MIP-Nd-TiO2 was investigated at calcination temperatures of 500°C and periods ranging from 1 to 4 h, as illustrated in Fig. 6(c). It is evident that increasing the calcination temperature from 1 to 2 h enhanced the MIP-Nd-TiO2 degrading performance, indicating that the calcination time was too short leading to the incomplete formation of anatase. The degradation performance of MIP-Nd-TiO2 gradually decreased with the time from 2 h to 4 h, indicating that the calcination time was too long leading to the formation of rutile-phase TiO2, which was unfavorable to the photocatalytic reaction. When the calcination time is 2 h, the formation of the anatase phase can be better and the photocatalytic performance can be improved, so the optimal calcination time of the catalyst is 2 h. Combined with the above, the optimal calcination conditions of MIP-Nd-TiO2 were obtained to be calcined at 500 ℃ for 2 h.
3.2.4. Adsorption properties of catalysts
Figure 6(d) shows the pure adsorption diagram of the catalysts. The degradation rates of OTC by TiO2, Nd-TiO2, and MIP-Nd-TiO2 were 3.74%, 9.98%, and 16.21%, respectively, after achieving the adsorption-desorption equilibrium of the three catalysts after 60 minutes of adsorption in the dark. The adsorption rate of pure TiO2 was negligible at less than 5%. In contrast, doping Nd and adding imprinted molecules enhanced adsorption performance, which might be attributed to an enhancement in the catalyst's specific surface area after doping Nd and adding imprinted molecules (following the results of Table 1), and the incorporation of the molecular imprints provided more selective active sites, which allowed for the adsorption of more pollutants.
3.2.5. Photocatalytic performance of catalysts
Figure 7(a) shows the photocatalytic degradation of the catalysts. It can be clearly found that the photocatalytic performance of MIP-Nd-TiO2 is much larger than its adsorption performance, which degrades OTC mainly through photocatalytic reaction. The degradation rates of TiO2, Nd-TiO2, and MIP-Nd-TiO2 on OTC were 64.34%, 76.67%, and 91.97%, correspondingly. MIP-Nd-TiO2 exhibited a 1.42-fold increase in degradation efficiency in comparison to pure TiO2. It suggests that doping with Nd and adding imprinted molecules improves the photocatalytic activity of pure TiO2 more than before. The degradation rate of OTC by MIP-Nd-TiO2 is enhanced by 15.5% compared with that of Nd-TiO2. It may be due to the formation of imprinted cavities after doped molecules imprinting, which provides recognition sites for OTC and can degrade OTC more efficiently.
3.2.6. Influence of different reaction conditions on the degradation performance of catalysts
(1) Influence of different initial concentrations of OTC catalysts on degradation performance
In daily life, the concentration of pollutants in wastewater can be different due to different production methods, so it is necessary to study the efficiency of the catalyst to degrade different concentrations of degradation. Figure 7(b) investigated the degradation rate of MIP-Nd-TiO2 for the degradation of different concentrations of OTC. The experimental procedure is the same as the photocatalytic experiment. The degradation rates of MIP-Nd-TiO2 for 10 mg/L, 20 mg/L, 30 mg/L, and 40 mg/L OTC were 95.50%, 91.97%, 84.03%, and 75.24%, correspondingly. It is evident that the concentration of OTC increased concurrently with a progressive reduction in the MIP-Nd-TiO2 degradation rate. This may be attributed to the fact that with the gradual increase of OTC concentration, on the one hand, the color of the solution gradually deepens, which reduces the light transmittance, and on the other hand, the light absorption is lower because more OTC molecules in solution are encapsulated on the surface of MIP-Nd-TiO2. These factors made the degradation performance of MIP-Nd-TiO2 decline.
(2) Influence of OTC at different pH on the degradation performance of catalysts
The pH of the wastewater may change every moment, so it is necessary to study the degradation rate of MIP-Nd-TiO2 when degrading OTC at different pH, It is evident from Fig. 7(c) that at pH = 6.65(pH of 20 mg/L OTC), MIP-Nd-TiO2 had the maximum degrading efficiency of 91.97%., and degradation efficiencies at pH = 3, 5, and 9 respectively were 79.93%, 87.16%, and 83.17%. As the pH of OTC rises, the degrading performance of MIP-Nd-TiO2 on OTC tends to first rise and then fall, which may be due to the fact that when the pH is lower, there is a strong positive charge in the solution; When the pH is higher, there is a strong negative charge in the solution, and the strong electrostatic repulsion between the charges significantly reduces the photocatalytic performance of the catalysts(Wu et al 2016). When pH = 6.65, the solution is neutral, there are fewer positive and negative charges in the system, and electrostatic repulsion is almost nonexistent(Shen et al 2023). As a result, the photocatalytic performance remains almost unchanged. So it shows higher photocatalytic performance.
3.2.7. Adsorption-photocatalytic synergistic reaction
In practical engineering, wastewater treatment often pursues the highest possible degradation efficiency. Through our study, we found that the efficiency of OTC degradation by MIP-Nd-TiO2 was higher under the adsorption-photocatalytic synergistic reaction. Figure 7(d) shows the degradation of OTC by three catalysts under the adsorption-photocatalytic synergistic reaction of MIP-Nd-TiO2, it can be seen that after 40 min of reaction, the degradation of OTC by pure TiO2, Nd-TiO2, and MIP-Nd-TiO2 degradation of OTC after 40 min of reaction were:64.44%, 77.19%, and 93.14%, correspondingly. This phenomenon occurs owing to the concomitant operation of adsorption and photocatalysis: catalysts containing adsorbed cavities have a greater propensity to absorb photons, thereby enhancing the movement of photogenerated electrons and subsequently augmenting their photocatalytic efficiency(Chen et al 2022). Compared with dark adsorption followed by photocatalytic reaction, the reaction time was 50 min less while achieving a better degradation effect and improving the efficiency of MIP-Nd-TiO2 in degrading OTC.
3.3. Molecularly imprinted Nd-TiO2 degradation selectivity studies
3.3.1. Adsorption selectivity
To investigate the selectivity of MIP-Nd-TiO2, tetracycline (TC), a structural analog of oxytetracycline hydrochloride (OTC), was selected as a competitive degradation pollutant for selectivity experiments. The adsorption selectivity of MIP-Nd-TiO2 was briefly investigated because of its much weaker adsorption performance compared to the photocatalytic ability. A 100 mL conical flask holding 50 mL of 20 mg/L OTC solution was filled with 0.01 g of MIP-Nd-TiO2, and the conical flask was placed into a thermostatic oscillator to oscillate for 3 h under dark conditions to test the final OTC concentration. The distribution coefficient KD and adsorption selectivity coefficient α1 were used to evaluate the adsorption selectivity of MIP-Nd-TiO2. Calculate the adsorption selectivity factor by listing the formula:
$${K}_{D}=\frac{{Q}_{e}}{{C}_{e}}$$
1
$${\alpha }_{1}=\frac{{K}_{D1}}{{K}_{D2}}$$
2
Where the competitor's and template's distributed factors are denoted by KD1 and KD2, accordingly.
α1 is the adsorption selectivity coefficient(Qi and Wang 2020).
Table 2
exhibits the fitting coefficient values. The adsorption selectivity coefficient of MIP-Nd-TiO2 and Nd-TiO2 for OTC are 1.392 and 0.895, correspondingly, in contrast to the adsorption selectivity coefficient of MIP-Nd-TiO2 for OTC, which are 1.55 times more than those of Nd-TiO2. It is demonstrated that MIP-Nd-TiO2 has superior adsorption ability for OTC compared to TC, indicating the selective adsorption of MIP-Nd-TiO2 on OTC.
Catalyst | Contaminants | Qe | Ce | KD | α1 |
MIP-Nd-TiO2 | OTC | 0.811 | 16.755 | 0.048 | 1.392 |
TC | 0.610 | 17.550 | 0.034 |
Nd-TiO2 | OTC | 0.499 | 18.003 | 0.027 | 0.895 |
TC | 0.550 | 17.790 | 0.031 |
Table 2 Adsorption selectivity and distribution coefficients of MIP-Nd-TiO2 and Nd-TiO2 for OTC
3.2.2. Photocatalytic selectivity
Figure 8(a) shows the degradation of OTC and TC by MIP-Nd-TiO2 and Nd-TiO2, respectively, and it can be clearly seen that both catalysts degraded OTC better than TC, but due to the blotting molecules doped in MIP-Nd-TiO2, the degradation of OTC by MIP-Nd-TiO2 was significantly superior to that of degradation of TC, whereas the degradation of OTC and TC by Nd-TiO2 degradation effects were very similar. Figure 8(b) shows the fitting of the photocatalytic reaction kinetics. it can be observed that the reaction kinetic constants, K, for the degradation of OTC and TC by MIP-Nd-TiO2, are 0.7756 and 0.4458, respectively, which is a very large difference, whereas there is a very small difference between the reaction kinetic constants, K, for the degradation of OTC and TC by Nd-TiO2. Furthermore, the photocatalytic selectivity of MIP-Nd-TiO2 for OTC was assessed using photocatalytic selection factors and selection coefficients. The kinetic constants of the two catalysts' photocatalytic processes are displayed in Table 3, the photocatalytic selectivity factors α2(Sharabi and Paz 2010), and the selectivity coefficient of R(Gadzekpo and Christian 1984). Where R and α2 are calculated as:
$$R=\frac{{K}_{1}}{{K}_{2}}$$
3
$${\alpha }_{2}=\frac{{R}_{1}}{{R}_{2}}$$
4
The higher selectivity factor represents the better selective degradation of OTC by the catalyst, and the selectivity factor of MIP-Nd-TiO2 for OTC is higher than that of Nd-TiO2, which is 1.653 times higher in comparison. It indicates that the doping of imprinted molecules improved the selectivity of the catalyst.
Table 3
Comparison of the main reaction kinetic parameters of photocatalyst
Catalyst | Contaminants | k/min− 1 | R | α2 |
MIP-Nd-TiO2 | OTC | 0.077 | 1.974 | 1.653 |
TC | 0.039 |
Nd-TiO2 | OTC | 0.043 | 1.194 |
TC | 0.036 |
Figure 8 (a) Photocatalytic degradation of OTC and TC with different catalysts, (b) Reaction kinetic fitting
3.4. Analysis of photocatalytic degradation mechanism·
Quenching experiments were performed to investigate the contribution of ·O2−, ·OH, and H+ to the photocatalytic reactions, with 0.15 mmol/L BQ, 1 mL t-BuOH, and 0.15 mmol/L EDTA-2Na as the trapping agents of ·O2−, ·OH, and h+, and Fig. 9(a) displays the outcomes of the quenching studies. It can be obviously seen that all three capture agents have some inhibition effect on the photocatalytic reaction, indicating that all three active substances play a role in the photocatalytic reaction, in which the inhibition of photocatalytic reaction is most obvious after the addition of BQ, compared with the degradation rate without any capture agent was reduced by 70.85%, which indicates that the ·O2 − plays a major role in the photocatalytic reaction. Figures 9(b), (c), and (d) illustrate the pattern obtained from the study using the electron spin resonance (ESR) technique, which can be associated with seeing that ·OH, ·O2 − and h+ all exhibited signals at 2 min of the reaction. This aligns with the findings of the quenching experiments, suggesting that all three active components contribute to the photocatalytic process.
Figure 10 illustrates the reaction pathway of the photocatalytic degradation of OTC using MIP-Nd-TiO2. MIP-Nd-TiO2 has visible light responsiveness, and after absorbing the light energy, it excites valence band electrons into the conduction band. At this time, the electron valence band jumps, getting a free electron (e−). The electron that is exiting the valence band will produce a "hole" (h+). The formation of electrons and holes occurs almost simultaneously, and together they form electron-hole pairs. However, to carry out an effective photocatalytic reaction, the electrons, and holes need to be separated to prevent them from compounding rapidly. h+ can directly oxidize the OTC molecules adsorbed on the surface of MIP-Nd-TiO2 or react with water to form ·OH, and in the meanwhile, reactive oxides like ·O2− can be created when e-reacts with oxygen molecules in solution or other oxidizing agents. Quenching experiments have proved that ·O2− is the main active species for photocatalysis. These ·O2− have strong oxidizing ability and can degrade the hygromycin molecule from the following two pathways: in the first pathway, the OTC molecule is deamidated and demethylated, followed by further oxidation, ─H═CO releases and opens the double bond, and then C═O will be oxidized and demethylated, and finally the double bond is broken to obtain P1-5. In the second pathway, the OTC molecule is stripped of H2O first to produce P2-1, the decarbonylation reaction produces P2-2, and further dehydration produces P2-3(Gao et al 2022). These two pathways eventually continue to break down into other small molecule compounds and eventually mineralize into CO2 and H2O.
3.5. Repeatable experiments
The treatment cost is a necessary consideration in practical applications, and the reuse of catalysts can reduce the cost to a large extent, therefore, the reuse rate of catalysts is an important index to examine the catalysts. To elucidate the impact on the deterioration of OTC when MIP-Nd-TiO2 is reused, four cycles experiments of MIP-Nd-TiO2 for OTC degradation under the same conditions were set up, the experiments were adsorption-photocatalytic synergistic reaction (same as above), and the degradation rate of OTC was tested for 40 min in each experiment. Before each cycle, the catalyst from the previous cycle is recovered, rinsed, and dried. The outcomes of four cycles are exhibited ed in Fig. 11. The degradation performance for OTC is weakened a little bit after each cycle experiment, which may be due to the fact that the catalyst cannot completely wash away the OTC molecules adhered to the surface of MIP-Nd-TiO2 during each cleaning, which not only the reactive sites of MIP-Nd-TiO2 is reduced but also the light absorption of MIP-Nd-TiO2 is reduced and thus the degradation rate of MIP-Nd-TiO2 to OTC decreases. It can be observed that after four cycles, the degradation rate of MIP-Nd-TiO2 on OTC is 82.1%, which is only 11.04% less than that of the first cycle, which indicates that MIP-Nd-TiO2 can be reused at a higher rate.