Open Access Article
Jiahao Wanga,
Lianyue Zhanga,
Haiyue Zhanga,
Runyu Caia,
Hengda Jina,
Man Xu*ac,
Xuan Cao
*abd and
Shuhua Yao*a
aShenyang University of Chemical Technology, Shenyang 110142, Liaoning, China
bSchool of Engineering, Westlake University, Hangzhou 310024, China
cInstrumental Analysis Center, Shenyang University of Chemical Technology, Shenyang 110142, China
dCenter for Interdisciplinary Research and Innovation, Muyuan Laboratory, Zhengzhou, Henan 450016, China
First published on 5th August 2024
The overuse of antibiotics in treating bacterial infections is a significant threat to the environment and human health. The utilization of visible-light-assisted peroxydisulfate (PDS) activation for eliminating organic pollutants is a promising approach. This study uses a straightforward hydrothermal method to prepare magnetically recyclable spherical Cu2O@Fe3O4. The efficacy of this material in removing antibiotic pollutants was assessed using simulated wastewater containing tetracycline (TC). TC removal was achieved by activating PDS with Cu2O@Fe3O4 as the visible light photocatalyst. Experimental findings revealed that under specific conditions—a pH of 9, a Cu2O@Fe3O4 concentration of 60 mg L−1, and a PDS concentration of 25 mg L−1—the removal rate of TC reached 97.67% after 30 min of irradiation. Moreover, Cu2O@Fe3O4 exhibited excellent recyclability, maintaining a removal rate of 93.33% after five recycling rounds. X-ray diffraction characterization of the Cu2O@Fe3O4 composite before and after cycling confirmed its robust stability and reusability. In situ X-ray photoelectron spectroscopy analysis showed that electrons migrated from Fe3O4 to Cu2O during the photocatalytic reaction, indicating the formation of an S-type heterojunction in Cu2O@Fe3O4. Free radical trapping experiments demonstrated the active involvement of ·OH, ·O2−, SO4˙− and h+ radicals in TC removal.
Various methods exist for removing antibiotics from wastewater, including adsorption treatment, biological treatment, and membrane processes.4,5 Advanced oxidation processes (AOPs) are a promising technology for the partial or complete mineralization of pollutants through highly active free radicals such as hydroxyl radicals (·OH), sulfate radicals (SO4˙−), and superoxide radicals (·O2−).6 Among these, the peroxydisulfate activation process generates SO4˙−, which has a higher standard redox potential (E0 = 2.5–3.1 V) compared to ·OH (E0 = 1.89–2.72 V), thereby exhibiting strong oxidation capability.7 Photo-assisted persulfate activation (PPA) is gaining significant attention owing to its environmental friendliness, sustainability, and excellent chemical stability. PPA is widely employed to degrade antibiotics in aquatic environments.
Photocatalysis is a novel and environmentally friendly advanced oxidation technology.8 For photocatalysts to be highly effective, they must have abundant active sites, broad spectral absorption, rapid separation and migration rates of photogenerated electrons and holes, and robust oxidation and reduction capabilities.9 Among these factors, the construction of heterogeneous junctions by combining semiconductors is recognized as one of the most promising approaches for achieving photocatalytic electron–hole separation through the electric field formed by the heterojunction.10 Heterogeneous photocatalysts exhibit distinct mechanisms for photogenerated carrier transfer, stemming from variations in preparation methods, energy bands, morphologies, and structures. Based on the diverse mechanisms of photogenerated carrier transfer, heterogeneous photocatalysts are generally categorized into I-, II-, Schottky-, Z-, and S-types.11 S-Type heterogeneous photocatalysts garner significant attention owing to their unique advantages.12,13 In S-type heterogeneous photocatalytic systems, incorporating internal built-in electric fields (IEFs) effectively regulates the direction of carrier migration, enhancing the oxidation and reduction capabilities and extending the lifetimes of photogenerated holes and electrons. Thus, establishing S-type heterogeneous junctions is an effective strategy for enhancing photocatalytic efficiency.
Thus far, cuprous oxide (Cu2O) has exhibited remarkable photocatalytic performance, boasting a band gap width aligning with the visible light wavelength range, rendering it directly excitable by solar light.14 However, its instability arises from a tendency to undergo an irreversible redox disproportionation reaction.15 On the other hand, magnetite (Fe3O4) demonstrates photocatalytic capabilities and possesses considerable magnetic properties, facilitating easy separation and recovery from the reaction system, resulting in its widespread adoption in photocatalysis.16 Khaled Benabbas et al. Employed a hydrothermal approach to fabricate a magnetically separable Fe3O4/CuO composite core–shell heterostructure photocatalyst. Fe3O4/CuO displayed remarkable optical characteristics, including a low band gap value and superior light absorption capabilities. Evaluation of its photocatalytic activity in DR89 removal under visible light irradiation showcased the superior performance of the Fe3O4/CuO composite, surpassing pure CuO and Fe3O4 by 11 and 8 times, respectively. Similarly, Alani et al. used the hydrothermal method to produce a visible-light-driven bio-templated magnetic copper oxide (CuO/C/Fe3O4) photocatalyst. They found that CuO/C/Fe3O4 outperformed spherical polyhedral Fe3O4 NPs in catalytic activity. Visible light exposure of the CuO/C/Fe3O4 photocatalyst increased the generation of hydroxyl radicals (·OH), superoxide anion radicals (·O2−), and the redox Fe3+/Fe2+ pair, thereby enhancing photodegradation performance.
In this study, we synthesized a magnetic Cu2O@Fe3O4 composite material via a thermal precipitation method. In situ X-ray photoelectron spectroscopy analysis showed that electrons migrated from Fe3O4 to Cu2O during the photocatalytic reaction, indicating the formation of an S-type heterojunction in Cu2O@Fe3O4. A comprehensive structural analysis of Cu2O@Fe3O4 was conducted utilizing scanning electron microscopy, X-ray diffraction techniques, and energy-dispersive X-ray spectroscopy. Additionally, we confirmed its magnetic nature and strong magnetic properties. Furthermore, we elucidated the optical absorption spectrum of Cu2O@Fe3O4 through UV-visible diffuse reflection spectroscopy. To assess the practical utility of the composite material, we employed a TC solution to simulate antibiotic wastewater. We applied the Cu2O@Fe3O4 composite material with sodium persulfate for efficient degradation. Under illumination, photogenerated electrons facilitate the in situ redox cycling of Cu(II)/Cu(I) in Cu2O@Fe3O4, significantly enhancing the activation efficiency of PDS and yielding more sulfate radicals (SO4˙−). Through this experimentation, we investigated the degradation mechanism and influential factors associated with the composite material, thus experimentally validating its potential for application in antibiotic wastewater treatment.
m (No. 227). Similarly, Fig. 1(b) exhibits characteristic peaks, with observed peaks at 2θ values of 18.3°, 30.1°, 35.4°, 37.1°, 43.1°, 53.4°, 56.9°, 62.5°, 65.7°, 70.9°, 74°, 75°, and 78.9° (marked as ‘◆’), aligning perfectly with Fe3O4 (PDF#99-0073). These peaks correspond to crystallographic planes (111), (220), (311), (222), (400), (331), (422), (511), (440), (531), (620), (533), and (444), indicating a face-centered cubic crystal structure. Moreover, peaks marked as “●” at 2θ values of 29.6°, 36.4°, 42.3°, 52.5°, 61.3°, 69.6°, 73.5°, and 77.4° are confidently assigned to diffraction peaks of cubic-phase Cu2O nanoparticles, corresponding to crystal planes (110), (111), (200), (211), (220), (310), (311), and (222) of Cu2O (PDF#99-0041), with a face-centered cubic crystal structure and space group Fd
m (No. 224). Based on XRD data analysis, it can be preliminarily concluded that the synthesized sample corresponds to the desired Cu2O@Fe3O4 composite material, confirming the successful implementation of the employed methodology.
For further analysis of the chemical composition and states of Cu2O@Fe3O4, X-ray photoelectron spectroscopy (XPS) was employed, with results presented in Fig. 2. Fig. 2(a) provides the XPS spectra, where distinct peaks for O1s, Fe2p, Cu2p, CuLM2, and other species are observed. In Fig. 2(b), the XPS spectrum of iron in the composite material is depicted, revealing binding energies of Fe2p1/2 and Fe2p2/3 orbitals at 722.93 and 709.23 eV, respectively, consistent with literature data for Fe3O4.17 Fig. 2(c) presents the energy spectrum of Cu2p in Cu2O@Fe3O4, showing Cu2p3/2 and Cu2p2/3 orbitals at 931.5 and 951.33 eV, respectively, with a 19.83 eV difference. The absence of significant satellite peaks between them suggests the presence of Cu2O in the prepared samples.18 As depicted in Fig. 2(d), the composite sample exhibits two distinct peaks in the 1s orbital of oxygen, with binding energies of 528.92 and 530.19 eV, corresponding to lattice oxygen and oxygen molecules adsorbed on Cu2O.19 These XPS results further corroborate the predominance of Fe3O4 and Cu2O in the processed samples.
Low-magnification scanning electron microscopy (SEM) images of the Cu2O@Fe3O4 nanoparticles are depicted in Fig. 3(a), showcasing spherical particles with a uniform size distribution, predominantly ranging from 1000 to 1800 nm. Further high-magnification observations (Fig. 3(b) and (c)) show that the composite particles comprise numerous smaller nanoparticles, resembling the reported Cu2O shell structure. The fabricated composite's surface composition and element distribution were quantitatively analyzed using energy-dispersive X-ray spectroscopy (EDS) techniques. Fig. 3(c)–(e) clearly show the uniform distribution of Cu, O, and Fe elements. Fig. 3(f) provides the atomic content of each element, indicating that Cu, O, and Fe constitute 17.81%, 13.12%, and 4.34%, respectively. Based on preliminary estimation, the Fe3O4 to Cu2O ratio is determined to be 1
:
3. The SEM-EDS spectrum further confirms the successful synthesis of composites incorporating Fe3O4 and Cu2O.
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| Fig. 3 (a)–(c) SEM images of Cu2O@Fe3O4; (d) SEM images; (e) EDS full spectrum; (f)–(h) single element distribution map: (f) Cu; (g) Fe; (h) O; (i) the atomic content of Cu, O, and Fe. | ||
Through vibrating-sample magnetometer analysis, magnetic measurements and studies were conducted on the Cu2O@Fe3O4 composite material. As depicted in Fig. 4, the composite material exhibits distinctive magnetic hysteresis loop characteristics. With the gradual increase of magnetic field strength, the material's magnetization increases, saturating at a magnetic field strength of approximately 1500 Oe. Analysis of Fig. 4 reveals the composite material's paramagnetic properties, with a residual magnetization of 2.7 emu g−1, a coercivity measurement of 95.7 Oe, and a saturation magnetization of 10.4 emu g−1. These characteristics underscore the composite material's high magnetic responsiveness and potential for separation and recovery, facilitating material recycling and reuse.
UV-Vis spectroscopy experiments were used to investigate the optical response of Cu2O@Fe3O4 composite materials. As Fig. 5(a) shows, Cu2O@Fe3O4 composite materials exhibited outstanding optical response. The composite materials demonstrated superior light absorption in the spectral range from 300 to 500 nm compared to pure Fe3O4. Employing the Kubelka–Munk relaxation function and UV-Vis spectroscopy, the energy gap of Cu2O@Fe3O4 was estimated to be 1.74 eV, which is lower than that of Fe3O4 (2.12 eV). Literature reports suggest that a reduction in the energy gap can expand the light absorption range, consequently enhancing photon absorption and the generation of photogenerated carriers. This ultimately results in improved utilization efficiency of visible light during photocatalytic processes.20
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| Fig. 5 (a) UV-Vis diffuse reflectance spectra of Cu2O@Fe3O4 and Fe3O4, (b) (αhν)2 and hν curves of Fe3O4@Cu2O samples, (c) (αhν)2 and hν curves of Fe3O4 samples. | ||
We employed photoluminescence spectra (PL), intermittent transient photocurrent response spectra, and electrochemical impedance spectroscopy (EIS) for a comprehensive understanding of photo-electrochemical carrier separation. Fig. 6(a) clearly illustrates that the photoluminescence spectra (PL) intensity of Cu2O@Fe3O4 is significantly lower compared to Fe3O4, indicating effective separation of photo-induced electrons and holes in the composite material.21 The photocurrent response of Cu2O@Fe3O4, as shown in Fig. 6(b), is nearly four times higher than that of Fe3O4. This intensified photocurrent enhances the separation of electrons and holes. Fig. 6(c) compares the EIS of Cu2O@Fe3O4 and Fe3O4, revealing that Cu2O@Fe3O4 exhibits a smaller arc radius than Fe3O4, facilitating the transfer of photogenerated carriers. The abovementioned results further improve the successful construction of Cu2O@Fe3O4 to avoid the combination of photo-induced electrons and holes. Therefore, this further confirms that Cu2O@Fe3O4 possesses superior photocatalytic performance compared to pure Fe3O4. The degradation effect of tetracycline was studied by Cu2O@Fe3O4 and Cu2O under light, and the results are shown in Fig. S2.† Found that Cu2O@Fe3O4 was superior to Cu2O in its degradation activity. Please watch the ESI† for detailed data.
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| Fig. 6 (a) Photoluminescence spectra, (b) intermittent transient photocurrent response spectra, and (c) electrochemical impedance. | ||
The impact of Cu2O@Fe3O4 dosage (20, 40, 60, 80, and 100 mg L−1) on the removal efficiency of TC was thoroughly examined. As depicted in Fig. 7(b), with the gradual increase in Cu2O@Fe3O4 dosage from 20 to 60 mg L−1, the removal rate of TC increases from 89.3% to 97.6%. However, upon further increasing the dosage to 80 mg L−1, the removal rate declines, dropping to 92.7%. Subsequently, at a dosage of 100 mg L−1, the removal rate rebounds to 93.9%. These findings suggest that the optimal Cu2O@Fe3O4 dosage for photocatalysis is 60 mg L−1. At lower concentrations, increasing the catalyst dosage enhances the removal efficiency of TC. However, when the dosage surpasses a certain threshold (e.g., from 60 to 100 mg L−1), the removal rate of TC decreases owing to light scattering, which reduces light absorption within the reaction system.
The initial pH of the solution plays a crucial role in TC removal. Thus, we investigated the impact of various pH values (5, 7, 9, 11, and 13) on the removal rate of TC under conditions of TC concentration at 20 mg L−1 and PDS concentration at 25 mg L−1. The outcomes of these experiments are presented in Fig. 7(c). Increasing the solution's initial pH from 3 to 9 led to a slight increase in the rate of pollutant elimination, albeit not significantly. However, when the pH increased from 9 to 11, the removal efficiency of TC by Cu2O@Fe3O4 composites considerably decreased from 97.6% to 43.1%. This decline indicates a decrease in the removal effectiveness of Cu2O@Fe3O4 composites at higher pH values. Such an effect may be attributed to the decelerated rate of chemical reactions or the onset of competing reactions under high pH conditions, thereby impeding the degradation process to some extent.
The impact of PDS dosage on TC removal was investigated, with the corresponding data presented in Fig. 7(d). The experiment was conducted at room temperature, utilizing a Cu2O@Fe3O4 dosage of 60 mg L−1 and a pH of 9. After 30 min, it was observed that within the range of 15–25 mmol L−1, the removal rate of TC exhibited an upward trend with increasing PDS concentration. This phenomenon can be attributed to the activation of PDS by photogenerated electrons or other free radical groups on the surface of Cu2O@Fe3O4, thereby enhancing TC removal capability. However, beyond a PDS concentration of 25 mg L−1, the removal rate of TC sharply declines. This decline may be attributed to potential competition that interferes with TC removal.
Various concentrations of TC (10, 20, 30, and 40 mg L−1) were examined to evaluate their influence on the removal rate under different initial TC concentrations. Fig. 7(e) illustrates that, at room temperature, with a Cu2O@Fe3O4 dosage of 60 mg L−1, a solution pH of 9, and a PDS dosage of 25 mg L−1, the initial TC concentration affects its removal rate. As the initial TC concentration increases from 10 to 20 mg L−1, the removal rate gradually increases from 96.5% to 97.6%. However, upon further increasing the initial TC concentration to 90 mg L−1, the removal rate declines to 20 mg L−1. The increased TC concentration makes the wastewater deficient in sufficient radical oxidation, significantly reducing the removal rate.
To assess the stability of Cu2O@Fe3O4, five cyclic reaction experiments were conducted under optimal conditions (room temperature, initial pH 9, TC dosage of 20 mg L−1, Cu2O@Fe3O4 composite catalyst dosage of 60 mg L−1, and PDS dosage of 25 mg L−1). The reacted Cu2O@Fe3O4 composite material was collected using a magnet, washed, dried, and reused for subsequent cycles. As depicted in Fig. 7(f), the TC removal rates for the five cyclic experiments were 97.6%, 97.2%, 97%, 95.8%, and 93.3%, respectively. These results indicate a gradual decrease in the TC removal efficiency of the Cu2O@Fe3O4 composite catalyst with increasing cycles. From the first to the fifth cycle, the TC removal rate consistently declined, suggesting a possible loss or deactivation of the catalyst's activity. This decline could be attributed to the blockage or damage of active sites on the catalyst surface, leading to reduced catalytic performance.
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| Fig. 9 (a) In situ XPS full spectrum image; (b) O1s spectrum image; (c) Fe2p spectrum image; (d) CuLM2 spectrum image; (e) Cu2p spectrum image. | ||
Under illumination, PDS undergoes activation, generating sulfate radicals (SO4˙−) directly, and can also be further activated by acquiring free electrons. During this process, photogenerated electrons facilitate the in situ redox cycling of Cu(II)/Cu(I) in Cu2O@Fe3O4, significantly enhancing the activation efficiency of PDS and yielding more sulfate radicals (SO4˙−). These radicals may partially convert to ·OH and ·O2− during the reaction, subsequently combining with water molecules or dissolved oxygen to form species with potent oxidizing ability.
Furthermore, when free photo-excited electrons react with dissolved oxygen (DO) molecules, ·OH and ·O2− radicals are also generated. These radicals play a crucial role in degrading organic pollutants. Simultaneously, photogenerated holes directly participate in the decomposition of TC, accelerating the separation of electrons and holes, thereby enhancing the overall photocatalytic efficiency.
The Cu2O@Fe3O4 sample demonstrates remarkable photocatalytic efficiency in the PDS activation system. Under the conditions of pH 9, composite material concentration of 60 mg L−1, and PDS concentration of 25 mg L−1, 97.67% of TC is removed within 30 min. The degradation efficiency remains consistent even after five rounds of recycling, showcasing the excellent recyclability of Cu2O@Fe3O4. Free radical trapping experiments revealed that the active radical species responsible for TC removal include h+, ·O2−, SO4˙− and ·OH.
Footnote |
| † Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4ra04174g |
| This journal is © The Royal Society of Chemistry 2024 |