Abstract
Cu1–xNixO/Fe2O3 (with x = 0.01, 0.02, 0.03, 0.04 wt%) were synthesized by plant extraction technique. The absorbance and degradation performance of Ni-doped CuO and Fe2O3 nanocomposite against methylene blue (MB) was analyzed, and the 2% Ni-doped CuO yielded an optimum result, and the optical bandgap of CuO, 2NCO, Fe2O3, and (60%) 2NCO/40% Fe2O3 was found to be 1.88, 1.73, 2.1, and 1.80 eV, respectively. Hence, the 2% Ni-doped CuO (2NCO) was further used for the establishment of a composite with Fe2O3. The lowest composition of the oxide composite was (1−x) 2NCO/(x) Fe2O3 (x = 0.1, 0.2, 0.3, 0.4, and 0.5). The degradation performance of those oxide composites was determined against (MB) with the nominal composition of sample (60%) 2NCO/40% Fe2O3 resulted in an optimum degradation of MB with a percentage of 94% at 120 min. The recyclability takes a look at was performed for five cycles at the start of 94%; after five cycles, the sample remained stable at 120 min. Therefore, 2NCO/40% Fe2O3 composite is going to be the selection material for waste product treatment.
1. Introduction
The need of eliminating organic contaminants and harmful heavy metal ions from water sources has increased in response to the rising demand for clean water [1]. MB is an organic contaminant that has devastating environmental effects due to its toxicity, carcinogenicity, mutagenicity, nonbiodegradability, and complex chemical structure. As a result, before they are released into the environment, these contaminants must be efficiently removed and/or converted to nontoxic molecules [2]. There are several techniques for removing and converting these contaminants have been developed. Some of these processes are flocculation [3], adoration [4], biodegradation [4], sedimentation [5], and membrane process [6]. Since contaminants have complex chemical and physicochemical properties. Those techniques have limitations of low efficiency, high-energy consumption, and the risk of secondary pollutant formation are insufficient [7]. Furthermore, due to the presence of stable aromatic groups in the structure of organic pollutants, they are nondegradable using traditional techniques [8]. As a result, an alternative technique for removing and converting toxic molecules and substances from industrial effluents that is high in efficiency, low in energy consumption, and environmentally friendly is desired. One of the alternative approaches to treating industrial contaminants is photocatalysis, which uses photon energy and oxide semiconductor nanomaterials as a catalyst to degrade organic contaminants [9]. Metal oxides such as TiO2 [10], ZnO [11], CeO2 [12], CuO [13], Fe3O4 [14], Fe2O3 [15], BiVO4 [16], and others have been studied for their photocatalytic activity due to the degradation of various organic pollutants. Catalysis by metal oxides under solar irradiation is primarily limited by a large bandgap, low charge transfer efficiency, and low recyclability. This limitation is improved by heterojunctions, metal or nonmetal doping. Green technology based on plants is becoming more popular as an eco-friendly, nontoxic, cost-effective, and safe option because plant extract-mediated biosynthesis of nanoparticles provides natural capping agents in the form of protein [17]. CuO and α-Fe2O3, two important transition metal oxides, have been extensively studied and applied in a variety of fields, including catalysts [18], sensors [19], and electrochemistry [20]. Many methods have been used to create CuO/Fe2O3 composites, including solid-phase reaction [21], hydrothermal [22], coprecipitation [23], sol–gel method [24]. The green synthesis method has advantages over other synthesis techniques due to its high yield, high product purity, no need for organic solvents, easy reproducibility, low cost, and environmentally friendly approach [25].
According to recent research, the photon property of CuO is important because of the variable oxidation states of copper, i.e., Cu+, Cu2+, and Cu3+, which allows for both hole and electron doping [26]. Many changes have been reported as a result of transition metal doping into the CuO lattice, including Ni, Fe, Ti, Cd, and Zn doping [27]. To overcome metal oxide’s limitations in photocatalytic applications. We designed a plant-mediated synthesis of Ni-doped CuO, and Fe2O3 is found to be an interesting material for increasing the absorption of visible light. Hence, within the bandgap, transition metal ions can generate energy states. Furthermore, these act as stepping stones for electrons as they transition between the valence and conduction bands [26, 28].
In this work, plant-mediated Ni-doped CuO and Fe2O3 composite have been used for the degradation of MB. Pristine CuO has low photocatalytic activity due to agglomeration and recombination problems. This problem was improved by doping with Ni with a similar ionic radius, forming a junction, and decreasing agglomeration by plant-mediated synthesis method of metal oxides. Moreover, there is no research has been conducted on photocatalyst material Ni-doped CuO and Fe2O3 by plant-type Acmella ciliata, which was used as a capping/stabilizing agent during the synthesis of metal oxide for MB dye degradations.
2. Results and Discussion
2.1. X-Ray Diffraction (XRD) Analysis
The detailed synthesis experimental procedures of all catalysts were explained on pages s1 and s2 of Supplementary Material. Figure 1(a) XRD patterns of CuO and p-CuO confirming that the synthesized individual oxides with a single phase. The diffraction peaks at 2θ of 32.51°, 35.56°, 38.92°, 46.47°, 48.84°, 53.68°, 58.4°, 61.6°, 66.3°, 68.16°, 72.46°, and 75.26° were corresponded to (110), (002), (111), (₋112), (₋202), (020), (₋113), (₋311), (31₋1), (220), (311), and (004) crystallographic planes, respectively. In accordance with JCPDS card no: 48-1548, Figure 1(a) depicts a cubic crystal structure with a space group of C2/c [29]. The plant extracts CuO exhibits similar diffraction peaks and crystallographic planes. As shown in XRD patterns in Figure 1(b) of Fe2O3, the diffraction peaks at 2 24.14°, 33.28°, 35.62°, 40.95°, 49.56°, 54.03°, 62.48°, 64.06°, 71.82°, 75.26°, and 77.26° corresponding to (012), (104), (110), (113), (024), (116), (018), (214), (300), (1010), and (220) planes, respectively. The Fe2O3 contains a tetragonal crystal structure with space group R-3c; the result observed was in close agreement with JCPD card no: 33-664 [30].
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The XRD patterns of Figure 1(c) p-CuO, 1NCO, 2NCO, 3NCO, and 4NCO with their percentage compositions that show no other extra impurities exist for the doping concentration of Ni with 1, 2, 3, and 4 wt% as containing a cubic crystal structure. Because of the substitution of Ni2+ (0.69) with Cu2+ (0.73) sites in their monoclinic structure by similar ionic radii. Furthermore, the addition of Ni dopant to the CuO lattice had no effect on the lattice and only caused a minor shift in the 2θ values, as shown in the XRD inset in Figure 1(c). Different concentrations of nickel dopant list, which is 1%–4% are found in Table S1.
The XRD patterns, as shown in Figure 1(d), the main diffraction peaks are at 2θ of 35.5°, 38.7°, 48.7°, 58.3°, 61.6°, 66.2°, and 68.2° correspond to (₋111), (111), (₋202), (202), (₋113), (₋311), and (200) crystallographic planes, with the result closely matching the standard CuO JCPDS card no: 48-1548 [31]. The XRD pattern also presented intense diffraction peaks at 2θ of 24.1°, 33.1°, 40.9°, 49.4°, 54.0°, 62.4°, and 64.0° correspond to the (012), (104), (113), (024), (116), (214), and (300) crystallographic planes, respectively, and the result matched with standard Fe2O3 JCPDS card no: 33-664 [32]. Nickel-doped copper oxide was prepared by adding 1 up to 4%, as shown in Table S1, and similar the synthesize procedure of composites was explained in percentage composition, also shown in Table S2.
The XRD patterns of Figure 1(c) p-CuO, 1NCO, 2NCO, 3NCO, and 4NCO show that there is no extra impurities exist for the doping concentration of Ni with 1, 2, 3, and 4 wt% containing a cubic crystal structure. Hence, the substitution of Ni2+ (0.69) with Cu2+ (0.73) sites in their monoclinic structure by similar ionic radii. Furthermore, the addition of Ni dopant to the CuO lattice had no effect on the lattice and only caused a minor shift in the 2θ values, as shown in the inset of Figure 1(c). The widening of XRD peak is due to the reduction in the crystallite size of CuO. Furthermore, there is no noticeable change in peak location, and the peaks are found to be fairly sharp and high intensity, implying that the produced powders have high crystallinity. The crystallite size was calculated using the Debye–Scherrer Equation (1) by measuring the full width at half maximum (FWHM) of the most intense diffraction peak [33].where β is the half-maximum intensity (FWHM) of the observed diffraction peak, k is the Scherrer constant 0.9 and λ is the X-ray wavelength (Cuk radiation = 0.154 nm). The crystallinity of bare CuO, 1NCO, 2NCO, 3NCO, and 4NCO is 18.53, 9.51, 8.63, 7.76, and 7.67 nm, respectively. Additionally, 2NCO/10FO, 2NCO/30FO, 2NCO/40FO, and 2NCO/50FO were 13.12, 8.41, 8.85, 8.33, and 7.69 nm, respectively. The peak intensity decreases linearly as the FWHM increases with increasing Ni doping concentrations, indicating crystallinity degeneration of the CuO. The Ni ions move inside the CuO lattice and settle into the vacancy. The charge imbalance and ionic radius mismatch between Cu and Ni ions cause lattice distortion. CuO crystallization quality will be affected even more [34].
2.2. Thermal Analysis
Figure 2(a)–2(c) shows the thermogravimetric analysis (TGA)-DTA curves of composites 2NCO/10FO, 2NCO/30FO, and 2NCO/40FO. The first endothermic peak (α region) for composites 2NCO/10FO, 2NCO/30FO, and 2NCO/40FO at a temperature around 75°C, with a weight loss of ∼2%, 10.14%, and 10.6%, respectively, and this was due to the evaporation of residual water molecules adsorbed on the catalyst’s surface [35, 36]. At a temperature around 300°C, the second step (β region) shows removal hydroxides with weight loss of around 6.76%, 19.73%, and 16.56% for 2NCO/10FO, 2NCO/30FO, and 2NCO/40FO, respectively. At a temperature of 300–550°C, a pronounced endothermic peak was observed in the third step (γ region), forming 2CNO/Fe2O3, respectively, and corresponding weight loss of ∼7.81%, 19.52%, and 18.63%, respectively [37].
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2.3. Fourier Transform Infrared (FTIR) Analysis
The functional groups and chemical structures of Acimella plant extract and powder CuO, Fe2O3, p-CuO, and 2NCO/40FO were discovered by analyzing the FTIR spectra, as shown in Figure 3. The broad peak centered at 3,436 cm−1 corresponds to the stretching vibration of O–H, and there is a broadening of O–H covalent bond peaks, indicating that bond lengths of O–H covalent bonds have increased due to their involvement in hydrogen bonding [38]. The peak at 875 cm−1 is due to C–H stretching vibration, and the strong band below 700 cm−1 is assigned due to Fe–O stretching mode. The peaks at 647.626 and 520 cm−1 correspond to the characteristic stretching vibrations of the Cu–O bond in monoclinic CuO NPs. The sample’s characteristic absorption bands at 555 cm−1 correspond to iron oxide stretching, while the bands around 560 cm−1 correspond to the Fe–O stretching mode of the Fe2O3 phase [39]. The other peaks observed in the spectra were caused by stabilizers and hydroxyls adsorbed on the surface of the oxide [40]. The Cu–O stretching mode was occurred due to the stretching along the (202) direction in CuO crystal peaks at around 439 and 445 cm−1 [41].
2.4. Morphological Analysis
The morphology of CuO, p-CuO, Fe2O3, and 2NCO/40FO samples was examined using a scanning electron microscope (SEM). Figure 4(b) shows that the plant extract synthesized CuO shows well dispersed and decreased agglomeration, whereas CuO synthesized without plant extract is aggregated and not well dispersed. Figure 4(a) SEM image of CuO, (b) p-CuO, and (c) Fe2O3, and it was clearly observed that catalysts synthesized without plant extract are agglomerated together, and this may block access to catalyst surfaces that result lower its performance toward the photocatalysis effect. Figure 4(d) shows that the composite 2NCO/40FO catalysts are well dispersed and particles small in size. The surface area and N2 adsorption/desorption isotherm of CuO, p-CuO, Fe2O3, and 2NCO/40FO show similar pore sizes, as explained in Table S3. The properties of being well dispersed, smaller particle in size, higher surface area, and higher pore volume provides access to the catalyst particle surfaces that may enhance its photocatalytic performance [37].
2.5. Ultraviolet–Visible (UV–Vis) and Optical Studies
Figures 5(a) and 5(b) show that the optical absorption spectra of the samples CuO, Fe2O3, 1NCO, 2NCO, 3NCO, 4NCO, 2NCO/10FO, 2NCO/20FO, 2NCO/30FO, and 2NCO/40FO, 2NCO/50FO exhibit band edge absorption peak at 367.44 nm, whereas Figure 6(a)–6(d) show that the optical bandgap values estimation of samples Fe2O3, CuO, 2NCO, and 2NCO/40FO is 2.1, 1.88, 1.73, and 1.80 eV, respectively, which is calculated using the Tauc relation Equation (2).
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Eg stands for optical bandgap energy, v for frequency, h for Planck’s constant, and A for a transition probability constant [42]. The bandgap value clearly indicates that 2NCO/40FO reduces the bandgap energy. The catalyst absorbs more light as the bandgap narrows, allowing electrons to readily jump from the valance to the conduction band, and the formation of electron and hole pairs is essential in the dye degradation process.
2.6. Photoluminescence (PL) Analysis
PL is used to study the separation of photogenerated charge carriers because the PL signal is generally caused by the recombination of photogenerated electron–hole pairs. From the comparative PL spectra presented in Figure 7 of synthesized CuO, 2NCO, Fe2O3, and 2NCO/40FO. The PL-exhibited emission peaks in the 424.94 nm region under an excitation wavelength of 270 nm [43]. The PL intensity of Fe2O3 and 2NCO was found to be lower than that of pure CuO, indicating that Fe2O3 and 2NCO had greater charge separation than bare CuO due to bandgap and surface defects or interstitial defects. Therefore, the decrease in PL intensity of 2NCO/40FO may imply a low e−/h+ pair recombination rate and high photon efficiency of the catalyst, explaining the rise in photocatalytic activity [44].
2.7. Electrochemical Impedance Spectroscopy (EIS) Studies
This EIS result was measured in 0.1 M Na2SO4, frequency of 0.1 Hz–100 kHz, and 10 mV applied potential versus Ag/AgCl/Cl− reference electrode to check the conductivity properties of the catalysts. The EIS Nyquist plot’s arc radius indicates that the interface layer resistance occurs at the electrode’s surface. Figure 8 shows that the arc radius decreases for samples 2NCO, Fe2O3, and 2NCO/40FO than CuO due to the increased dipole moment; 2NCO/40FO has a lower arc radius than the other. During photocatalytic reaction tests, the composite 2NCO/40FO allows for faster charge separation and transfer of photogenerated charge carriers. The PL result in Figure 7 confirms that composite 2NCO/40FO has better charge separation. Hence, the obtained composite lowers the photogenerated electron–hole pair recombination, which results high photocatalytic activity toward dye degradation [45–47].
2.8. Photocatalytic Dye Degradation
The UV–Vis spectroscopy was used to examine the degradation percentage (D%), which is calculated by using Equation (3).where C0 and Ct are the dye concentrations at 0 and t minutes of irradiation, respectively. The absorbance versus wavelength plot was calculated using the Beer–Lambert rule using equation S4 and UV–Vis absorption spectra of MB solution at different light exposure time durations. The degradation efficiency, as shown in Figure 9 calculated using Equation (3) and for (a) CuO (68%), (b) p-CuO (74%), (c) 2NCO (81%), (d) Fe2O3 (84%), (e) 2NCO/40FO (94%). Figure S1 shows the degradation efficiency of (a) 1NCO (76%), (b) 3NCO (78%), (c) 4NCO (77%). The degradation efficiency of (a) 2NCO/10FO (81%), (b) 2NCO/20FO (84%), (c) 2NCO/30FO (86%), and (d) 2NCO/50FO (90%) at 120 min and UV–Vis absorption spectra of MB solution at different light exposure time durations of (a) 1NCO, (b) 3NCO, and (c) 4NCO, as shown in Figures S1 and S2. The photocatalyst efficiency of CuO was lower than CuO synthesized with plant extract. The plant-extracted CuO improved the surface area and charge carriers for MB dye degradation [48]. On the other hand, doping increases the photocatalytic activity of the catalyst by concentrating the target molecules (organic pollutants) at the catalyst surface by forming a Lewis acid–base combination, and as the doping concentration is increased, the degradation efficiency increased up to 2% Ni and then decreased and the optimum level of Ni-dopant is 2%. The use of Ni-dopant at the donor level avoids the recombination of excited electrons and holes in the valance band within the semiconductor. The crystalline size calculated from XRD result by Sherer’s Equation (1) and the 2NCO shows that optimum crystallinity due to its comparable effect. The crystalline size should be neither large nor too small; it should be optimum and comparable with its surface area. Figure 5(a) shows that the absorbance of 2NCO has high absorption property. Hence, the catalyst easily absorbs light and makes electrons travel from the valance band to the conduction band more than the others [49]. The composite of 2NCO/40FO was more efficient than the others due to the existence of secondary metabolites present in plant extract and metal ions present in the composite.
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2.9. Kinetics Study
The photodegradation rates of MB were faster with 2NCO/40FO composite than bare CuO under the same conditions, as shown in Figure 10(a). The pseudo 1st order model was used to study the kinetic degradation of MB dye photodegradation at neutral pH utilizing CuO, p-CuO, Fe2O3 2NCO, and 2NCO/40FO composite using Equation (4).where Ct is the MB concentration at irradiation time t, C0 is the preirradiation concentration, K is the first order rate constant (min−1), and T is the temprature [50]. Then plotting ln (Ct/C0) vs. t as shown in Figure 10(b) and the value of reaction rate was exhibited in Figure 10(c) was calculated for CuO, p-CuO, 2NCO, Fe2O3, and 2NCO/40FO, to be 0.00969, 0.01147, 0.01322, 0.01498, 0.02301, 0.77079, 0.84899, 1.619 1.57458, and 3.35464 min−1, respectively. 2NCO/40FO shows a higher kinetic rate than pure CuO, and the introduction of Fe2O3 in 2NCO can further increase to some extent. The data fitted well and gave a correlation coefficient of CuO, p-CuO, 2NCO, Fe2O3, and 2NCO/40FO, 0.93705, 0.93844, 0.94696, 0.94711, and 0.95389 at the neutral pH, respectively.
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2.10. Stability and Recyclability
For pilot-scale remediation systems, recovery and reusability of the photocatalyst are important parameters to be considered. Figure 11 depicts the recyclability and stability of the 2NCO/40FO catalyst after five cycles for 120 min reaction, and it is 0.125 g catalyst in 500 ml of the MB dye. This clearly indicated that the catalyst was recycled and reused after MB dye degradation. In the high-efficiency cycles, the performance of 2NCO/40FO attended from 94% to 80% after five cycles. There is a material loss during the recovery process (washing and drying), leading to a reduced dose in succeeding cycles, lowering surface catalytic activity and lowering performance [51]. The recyclability and stability test showed the catalyst was stable for up to five cycles. The XRD results of reused catalyst showed the reused material showed no change in crystal structure in the XRD pattern. In keeping with the findings, current materials systems degrade an organic MB dye from industrial effluents created by numerous processes. Therefore, the 2NCO/40FO photocatalyst was no significant change up to five cycles successfully for degrading of MB dye under visible light irradiation.
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2.11. The Proposed Dye Degradation Mechanism of 2NCO/40FO Nanocomposite
The photocatalytic mechanism of CuO/Fe2O3 composites is depicted in Figure 12. During UV light irradiation, electrons from the CuO and Fe2O3 valence bands (VB) are promoted to the conductive band (CB), leaving holes in the VB (h+ VB). The heterostructure creates a good couple, which helps separate the created electron–hole pairs [52]. CuO was doped with (2%) Ni to improve its electron transport properties. The difference in conduction band levels, electrons stored in the CuO conduction band travel to the Fe2O3 conduction band. Furthermore, the reaction between absorbed oxygen (O2) and electrons collected at the surface of Fe2O3 results in the formation of superoxide radical (·O2−) as electrons in Fe2O3 conduction band reduce absorbed O2. The MB dye was degraded by the superoxide radical and electrons that were generated [53]. However, the valence band holes in CuO and Fe2O3 barely met the criteria for the generation of hydroxyl radicals (·OH) (H2O/·OH−) instead (·OH) formed from the intermediate reaction shown in the following equations. The holes and hydroxyl radicals may play a role in the degradation process, as shown in the equations below. Finally, the process produced intermediate molecules such as H2O and CO2.
3. Conclusion
In the present work, CuO, p-CuO, Fe2O3, 1NCO, 2NCO, 3NCO, 4NCO, 2NCO/10FO, 2NCO/20FO, 2NCO/30FO, 2NCO/40FO, and 2NCO/50FO catalyst were successfully synthesized by plant-mediated extract, which is green synthesis method. The prepared materials were characterized by XRD, TGA, FTIR, PL, and EIS. The 2NCO/40FO catalyst shows lowered recombination and better charge transfer resistance. The performance of bare CuO was 68%, while the plant-extracted green synthesized CuO shows better degradation performance, and the synthesized Fe2O3 showed a degradation percentage of 81% and optimization of Ni-doped copper oxide with a doping concentration of 2% Ni-doped CuO was 80% maximum absorbance properties. The boosted photocatalytic property was assessed by coupling 2NCO coupled with Fe2O3 with weight percentages of 40% Fe2O3 with 2NCO/40FO was shown 94% and better absorbance properties. The recyclability and stability test showed the catalyst was stable up to five cycles, and the XRD result of reused catalyst showed no change in the XRD pattern. Consequently, the material will degrade organic MB dye, which is from different textile industrials effluents.
Data Availability
The finding of this study is supported by supplementary data and main manuscript (article).
Conflicts of Interest
The authors declare that they have no conflicts of interest.
Acknowledgments
We acknowledge the Adama Science and Technology University for funding and materials support.
Supplementary Materials
The experimental part. (Supplementary Materials)