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Article

ZnO and ZnO/Ce Powders as Tribocatalysts for Removal of Tetracycline Antibiotic

by
Dobrina Ivanova
1,
Hristo Kolev
2,
Bozhidar I. Stefanov
3 and
Nina Kaneva
1,*
1
Laboratory of Nanoparticle Science and Technology, Department of General and Inorganic Chemistry, Faculty of Chemistry and Pharmacy, University of Sofia, 1164 Sofia, Bulgaria
2
Institute of Catalysis, Bulgarian Academy of Sciences, Acad. G. Bonchev St., bl. 11, 1113 Sofia, Bulgaria
3
Department of Chemistry, Faculty of Electronic Engineering and Technologies, Technical University of Sofia, 8 Kliment Ohridski Blvd, 1756 Sofia, Bulgaria
*
Author to whom correspondence should be addressed.
Inorganics 2024, 12(9), 244; https://doi.org/10.3390/inorganics12090244
Submission received: 28 July 2024 / Revised: 26 August 2024 / Accepted: 4 September 2024 / Published: 5 September 2024
(This article belongs to the Special Issue Metal Catalyst Discovery, Design and Synthesis)
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Abstract

:
Research on tribocatalysis, which involves the triboelectric effect, is based on the concept that friction between dissimilar materials can generate charges capable of initiating catalytic reactions. This phenomenon holds significant potential for the degradation of wastewater contaminants in the environment. In this study, pure and Ce-modified (2 mol%) ZnO powders were investigated as tribocatalysts for the degradation of doxycycline (DC), a tetracycline antibiotic, in the absence of light. The research demonstrates that friction between the catalyst, the beaker, and the polytetrafluoroethylene (PTFE) magnetic rod induces charge transfer at their interfaces, leading to the breakdown of pollutants. Additionally, doxycycline degradation was observed at three different stirring speeds (100, 300, and 500 rpm). The results confirmed the tribocatalytic effect, showing that DC degradation increases with higher stirring speeds. Using ZnO and ZnO/Ce powders, maximum degradations of 80% and 55%, respectively, were achieved in 24 h at a stirring speed of 500 rpm. The findings of this study suggest that these samples can effectively degrade contaminants in water through the application of mechanical energy.

1. Introduction

Wastewater treatment is a critical aspect of human society’s development [1,2,3]. Several approaches exist for treating sewage, including photocatalysis [4,5,6,7,8], biodegradation [9], and adsorption [10,11,12]. While these methods are effective, each has inherent drawbacks. Chemical precipitation [13] can lead to secondary pollution, electrochemical methods are power-intensive and economically burdensome, biodegradation requires a prolonged degradation cycles [14,15], and photocatalysis suffers from low solar energy utilization rates and the easy recombination of photogenerated carriers [16,17,18]. Additionally, adsorption selectively adsorbs pollutants without decomposing them [19]. Therefore, it is essential to explore more effective and sustainable wastewater treatment techniques, such as tribocatalysis, based on the utilization of mechanical and frictional energy, which, like light energy, may be supplied via green energy sources widely used in industrial production.
Tribocatalysis is a mechano-electrochemical advanced oxidation process which employs the triboelectric effect—generating charges upon the frictional energy transfer between dissimilar surfaces, which in turn may react with water molecules, dissolved oxygen, and hydroxide ions in the aqueous phase, generating highly active free radicals, such as O2•− and OH•. These radicals are effective in pollutant removal due to their potent oxidizing properties. Although tribocatalysis, or frictional catalysis, is still relatively unexplored in the literature, it has already garnered significant interest. Lei et al. [20] demonstrated that BiOIO3 could catalyze the degradation of Rhodamine B (RhB) by over 90% in less than six hours by converting frictional energy into electrical charges and, subsequently, chemical energy. Another study by Gaur et al. [21] used calcium copper titanate nanoparticles with strong tribocatalytic activity to degrade cationic organic dyes such as RhB and MB. However, research on the application of tribocatalysis in the degradation of pharmaceutical products remains limited.
Antibiotics released into the environment from sources such as livestock excrement, hospitals, households, and pharmaceutical industries are contributing to the proliferation of bacterial strains resistant to current treatments, posing challenges for ecosystem management [22,23]. After ingestion, antibiotics undergo metabolism, but prolonged exposure can lead to mutagenic effects, nephropathy, spermatogenesis effects, arthropathy, photosensitivity, and damage to the central nervous system in organisms [24]. Thus, pollutants in wastewater must be fully mineralized. Doxycycline is an example of such an antibiotic.
Doxycycline (DC), a member of the tetracycline antibiotic family, is used in both human and veterinary medicine to treat Gram-positive and Gram-negative bacteria [25]. It consists of three functional groups: dimethylamine, tricarbonyl amide, and phenolic diketone [26]. Due to its chemical stability, DC is not biodegradable [26,27], making advanced oxidation processes a reliable method for breaking down these persistent pollutants.
This study investigates the degradation of doxycycline through tribocatalysis (friction catalysis) in the absence of light. We utilized hydrothermal ZnO and ZnO/Ce powders as tribocatalysts and evaluated their properties under stirring conditions. Factors, such as cerium ion incorporation, magnetic stirring speed, and the recyclability of modified samples were assessed to understand their influence on tribocatalysis in the degradation of tetracycline antibiotics.

2. Results and Discussion

2.1. Characterization of the Pure and Cerium Modified ZnO Powders

ZnO and ZnO/Ce powders were subjected to X-ray diffraction (XRD) analysis to investigate the crystal structure of the samples (Figure 1). Intense diffraction peaks at 2θ = 31.94°, 34.67°, 36.51°, 48.23°, 56.84°, 63.22°, 67.53°, and 68.18° indicate that the pure semiconductor is in the hexagonal wurtzite crystalline phase. These peaks correspond to the lattice plane orientations with hkl values of (100), (002), (101), (102), (110), (103), (112), and (201) [28].
The peak locations are consistent with the data from JCPDS Card No. 36-1451, confirming the absence of impurities or phase changes in the crystalline structure of the powder. The strong, sharp peaks in the XRD patterns of both pure and ZnO/Ce samples indicate a high degree of crystallinity. The nearly identical XRD patterns of the ZnO catalyst before and after cerium modification suggest that the crystal structure remains unchanged [29]. The absence of a distinct ceria phase in the modified ZnO composite can be attributed to its low concentration (2 mol%). Notably, ZnO modified by Ce shows a slight increase in the average crystallite size compared to pure ZnO, as determined by the Scherrer equation using the main peak (101). The modified ZnO catalyst has crystallite sizes of about 44 nm, while pure ZnO has a size of 37 nm. The XRD data demonstrate that the addition of cerium ions (2 mol%) does not significantly alter the crystal size. The crystalline lattice parameters remain unchanged after modification: ZnO (a, b = 3.250 Å; c = 5.206 Å) and ZnO/Ce (a, b = 3.248 Å; c = 5.205 Å). Powders modified with cerium ions retain their hexagonal wurtzite structure, as indicated by the calculated lattice parameters, which closely resemble those of ZnO.
Additionally, when the microstrain of the powders is computed using the c-axis lattice parameter, a positive value indicating tensile strain is observed. The tensile strain in the modified sample (7.33 × 10−4 a.u.) is slightly lower than that in ZnO (8.57 × 10−4 a.u.).
Scanning electron microscopy (SEM) was used to analyze the microstructure and morphology of the pure and modified samples (Figure 2). The SEM images revealed that the ZnO sample contained particles of various shapes. According to the images, the average particle size for ZnO was 0.25 µm, while for Ce-modified samples, it was approximately 0.5 µm. The SEM analysis indicates that morphology is not significantly affected by the Ce-modification, due to the low treatment temperature (100 °C).
Energy-dispersive X-ray spectroscopy (EDS) was used to determine the presence of Zn, O, and Ce in the modified ZnO/Ce powder (Figure 3). Peaks representing zinc, oxygen, and cerium can be observed in the spectrum. It was found that Ce has a weight percentage of approximately 3 wt.%. The high purity of the initial ZnO is supported by the absence of impurity peaks in the EDS spectrum (Figure 3a). The mapping data in Figure 3b show that cerium is uniformly distributed across the ZnO surface.
Additionally, transmission electron microscopy (TEM) was used to observe the shape and location of the ceria phase on the ZnO surface. The resulting micrographs are shown in Figure 4. The TEM images confirm that the tribocatalysts consist of polycrystalline agglomerates approximately 0.25 μm in diameter, consistent with the SEM analysis, representing the ZnO phase (Figure 4a). The ZnO tribocatalyst was covered by the Ce-oxide phase, visible as surface-bound particles approximately 10 nm in diameter in the higher magnification images (Figure 4b). These images also reveal an interplanar spacing of 0.27 nm, consistent with the (100) plane of CeO2 [30].
The chemical states of the pure ZnO and ZnO/Ce tribocatalysts were analyzed using X-ray photoelectron spectroscopy (XPS). The high-resolution XPS spectrum of the Zn 2p core-level region of pristine ZnO (Figure 5a) shows a peak at a binding energy (BE) of 1021.7 eV, corresponding to Zn 2p3/2, along with an accompanying peak associated with 2p1/2 at approximately 1044.7 eV. In the ZnO/Ce sample (Figure 5c), this peak remains largely unchanged, indicating no significant interaction between the precursor and substrate. The O 1s core level region, depicted in Figure 5b, was deconvoluted to reveal XPS doublet peaks at 530.3 eV and 531.6 eV, corresponding to lattice oxygen and extraneous (non-lattice and/or oxygen vacancies) oxygen in wurtzite ZnO [31]. For the ZnO/Ce modification, the Ce 3d core level region (Figure 5e) displays three sets of peaks: two well-separated triplets peaking at 882.2 eV and 898.1 eV, along with a Ce4+-satellite peak at 916.5 eV. These peaks correspond to the Ce 3d5/2 and Ce 3d3/2 core levels and are consistent with the formation of Ce(IV) oxide [32], indicating that the Ce3+ precursor was oxidized during preparation. Additionally, deconvolution of the O 1s region for the ZnO/Ce sample (Figure 5d) revealed a new low-intensity component at 529.5 eV (~6 at.%), which aligns with the formation of CeO2. The decreased intensity of the 531.7 eV peak, compared to the pure ZnO sample, is associated with oxygen vacancies and/or non-lattice oxygen in the ZnO structure, consistent with observations in other CeOx/ZnO nanocomposites [33]. The peak at 530.5 eV is again ascribed to the oxygen bonded with Zn, while the peak at 532.7 eV is associated with adsorbed water. The overall Ce(IV) concentration was determined to be 2.61 at.% (0.44 times less the oxygen associated with Ce-O bonds, close to the expected 0.5 ratio in CeO2), which is consistent with the full incorporation of the approximately 2 mol% cerium precursor used to functionalize the tribocatalytic ZnO/Ce nanocomposite.
Raman spectroscopy was used to confirm the phase composition of the ZnO materials, and Figure 6 shows the resulting spectra. The E2(high)-E2(low) mode of ZnO, the E2(high) mode, and the 2A1(low) + 2E2(low) broad band, correspond to the most intense Raman bands in all cases, appearing at 331, 439, and 1154 cm−1, respectively [34]. These results support the presence of wurtzite ZnO and do not indicate any significant alteration of the primary tribocatalyst component as a result of functionalization.

2.2. Tribocatalysis for the Degradation of Doxycycline via ZnO and ZnO/Ce Powders

The tribocatalytic activity of ZnO and ZnO/Ce powders was investigated by the degradation of the antibiotic doxycycline (DC) in darkness, using a magnetic stirrer with a PTFE magnetic bar at 300 rpm. All friction tests employed the same drug concentration (15 mg/L). The concentration of the drug solution was determined by measuring the distinctive absorbance of the DC molecule at a wavelength of 275 nm.
As shown in Figure 7, the concentration of the pollutant only slightly decreases when no catalyst is used and no stirring is applied. This result demonstrates that the tribocatalytic process is not significantly impacted by the friction between the glass beaker and the magnetic bar. Degradation of doxycycline is only observed in the presence of ZnO and ZnO/Ce tribocatalysts. After 24 h of magnetic stirring, the concentration of DC gradually decreased, signifying the degradation of the drug.
Figure 7a illustrates the tribocatalytic decomposition of the DC solution using pure and Ce-modified ZnO powders that were annealed at 100 °C. The degradation results confirm the tribocatalytic action, with 66.67% and 30.42% of the drug being degraded by the ZnO and ZnO/Ce powders, respectively, after a 24 h friction period.
The ZnO/Ce powder exhibits lower catalytic efficiency compared to pure ZnO. The trend is corroborated by the rate constant values (Figure 7b), calculated using the equation ln(Ct/C0) = −kt. The ZnO sample demonstrates a higher reaction rate (k = 0.0483 h−1) compared to the cerium-modified sample (k = 0.0168 h−1).
A possible diagram of the tribocatalysis principle is depicted in Figure 8. Positive (q+) and negative (q−) charges are produced on the surfaces of the ZnO powders and the PTFE stirring rod when the ZnO catalyst is stirred and subjected to friction [35]. ZnO, excited by friction, generates positive and negative charges. Triboelectrically generated electric charges can also achieve DC decomposition, similar to photocatalytic drug decomposition based on photogenerated carriers. Superoxide radicals (O2•−) are produced when oxygen molecules react with negative charges, while the positive charges on the surface of the ZnO powders are released into the water, producing active OH• radicals [35,36,37,38]. These radicals further break down the antibiotic tetracycline into inorganic compounds like carbon dioxide and water. Other studies have found that the presence of Ce ions in the structure of ZnO photocatalysts may act as recombination centers for photogenerated charges via electron trapping, leading to energy loss [37]. It is plausible that a similar mechanism could be operating in the ZnO/Ce tribocatalysts in this study. In the case of cerium, fewer positive and negative charges are produced on the surface of the modified sample and the PTFE rod, resulting in fewer active radicals and a slower degradation rate of the drug.
To further confirm the involvement of hydroxyl and superoxide radicals, a radical scavenger assay was conducted (Figure 9).
The contribution of superoxide (O2•−) and hydroxyl (OH•) radicals to the degradation of doxycycline was measured by incorporating scavengers such as ascorbic acid (AA) and isopropyl alcohol (IPA), which bind to the corresponding reactive species [39,40,41,42]. As shown in Figure 9, both tribocatalyst systems responded similarly to the addition of AA and IPA. However, in the case of AA, a more pronounced inhibition was observed, indicating that the generation of the superoxide radical plays a greater role in the DC tribodegradation rate.

2.3. Tribocatalysis for Degradation of Doxycycline via Different Magnetic Stirring Speeds

ZnO and ZnO/Ce powders were employed in tribocatalytic reactions for the degradation of doxycycline (DC) at different rotational speeds: 100, 300, and 500 rpm. The mixture was continuously stirred for 24 h, during which the drug concentration progressively decreased. The tribocatalytic characteristics of ZnO and ZnO/Ce powders regarding the effect of stirring speed on the DC degradation are illustrated in Figure 10. At 100, 300, and 500 rpm, the tetracycline antibiotic was degraded by 49.2%, 66.7%, and 80.4%, respectively, in the presence of pure ZnO (Figure 10a).
In all three cases, the Ce-modified powder exhibited poorer catalytic performance for drug decomposition. An increase in magnetic stirring speed accelerated the breakdown of the tetracycline drug. The rate constant (k) increased with faster rotation speeds, leading to improved catalyst efficiency (Figure 10b). Higher values of k and a greater degree of tribodegradation (Table 1) indicate a faster elimination of doxycycline due to the enhanced excitation of electrons (e−) and the oxidation of the organic pollutant at higher rotation speeds.
The degradation of DC was tracked using UV/Vis spectroscopy, monitoring the absorbance maxima at 275 nm. The UV/Vis spectra for DC degradation using pure ZnO and ZnO/Ce at 500 rpm are shown in Figure 11.
The tribocatalytic results at a rotation speed of 500 rpm were confirmed by Total Organic Carbon (TOC) analysis. TOC measurements were carried out to assess the degradation of doxycycline after 24 h of magnetic stirring in the dark, as shown in Figure 12. The TOC percentages for the decomposition of DC were 65.37% and 43.62% for the ZnO and ZnO/Ce powders, respectively. The TOC removal percentages of the tetracycline antibiotic were slightly lower than their decomposition rates during the tribocatalytic processes. This discrepancy was attributed to the formation of intermediate byproducts.
Compared to UV–vis spectroscopy, the TOC measurements revealed lower values of doxycycline removal. This discrepancy indicates the presence of multiple intermediate products involved in the complex multistep process of mineralization. For instance, during the drug’s photocatalytic oxidation, S. Pourmoslemi identified several intermediate products [43]. When interacting with the hydroxyl and superoxide radicals generated during the catalytic process, each of these byproducts possesses a distinct oxidation potential. Consequently, each intermediate will mineralize at a different rate, which is more easily detected during TOC analysis.

3. Materials and Methods

Materials: Commercial zinc oxide powder (>99.0%), cerium nitrate hexahydrate (Ce(NO3)3·6H2O, >99.0%), and absolute ethanol (C2H5OH) were obtained from Fluka (Burlington, MA, USA).
Doxycycline (DC, C22H24N2O8, λmax = 275 nm, Teva, Bulgaria) was selected as the model pollutant for the tribocatalytic experiments due to its widespread use and potential environmental impact. Doxycycline, a member of the tetracycline antibiotic class, is commonly used to treat various infections, including those of the skin, eyes, urinary tract, and respiratory system.
Synthesis of ZnO/Ce Powders: ZnO/Ce powders were synthesized using a simple and eco-friendly hydrothermal process. To prepare Ce-modified tribocatalysts, commercial ZnO powder and Ce(NO3)3.6H2O (2 mol%) were combined in a glass vessel, with ethanol added as the mixing medium. The mixture was stirred for 10 min, sonicated for 30 min, and then dried at 100 °C for 1 h to obtain the ZnO/Ce powders used in tribocatalytic testing.
Characterization Techniques: X-ray diffraction (XRD), to obtain the crystalline structure and phase composition of the as-prepared tribocatalysts, was performed on a Siemens D55 diffractometer (Karlsruhe, Germany) with CuKα radiation in the 2θ range of 25–75°. Mean crystallite dimensions and stress were evaluated through Rietveld analysis using PowderCell software, version 2.4. [44]. The surface morphology of the pure and Ce-modified ZnO was analyzed via scanning electron microscopy (SEM) on a JSM-5510 SEM (Krefeld, Germany) at an acceleration voltage of 10 kV. Energy-dispersive X-ray spectroscopy (EDX) for elemental analysis and chemical composition was performed using a Quantax 200 EDX detector (Bruker, Berlin, Germany) with a resolution of 126 eV. Transmission electron microscopy (TEM) analysis was conducted using a JEOL JEM-2100 microscope (Tokyo, Japan) at 200 kV. X-ray Photoelectron spectroscopy (XPS) was performed with an ESCALAB MkII spectrometer (Thermo Scientific, Manchester, UK) using a non-monochromated AlKα X-ray source (excitation energy: 1486.6 eV). The base pressure was 5 × 10⁻10 mbar, and the instrumental resolution was approximately 1 eV. Data were analyzed using SpecsLabII CasaXPS software (version 2.3.25PR1). Raman spectra were obtained using a ThunderOptics Eddu TO-ERS-532 spectrometer (Montpellier, France) with a 20× microscope objective lens and a 532 nm laser source.
Tribocatalytic Experiments: Tribocatalytic tests were conducted in a 100 mL glass beaker with a magnetic stirrer. A 50 mL solution of DC (15 ppm) in distilled water was used as the test medium. The tribocatalytic reactions were carried out at room temperature (23 ± 2 °C) in the absence of light. For each experiment, 50 mg of either pure or Ce-modified ZnO catalyst was added to the DC solution, and a PTFE-coated magnetic bar (ø 8 mm, L = 35 mm) was used for stirring. The mixture was allowed to reach adsorption equilibrium between the tribocatalysts and the DC solution by standing for 30 min without stirring. The magnetic stirrer was then activated, rotating initially at 300 rpm. Aliquots (2 mL) of the reaction solution were periodically collected, and the tribocatalyst was separated by centrifugation at 6000 rpm. The aliquots were analyzed using UV-Vis spectroscopy in the 200–450 nm range. This procedure was repeated under different magnetic stirring conditions (100 and 500 rpm).
Control Experiments: Additional tests were conducted without catalysts and without PTFE stirring to verify that no significant removal of doxycycline occurred under these conditions.
Scavenger Assay: To identify the reactive species involved in the DC degradation, scavenger tests were performed using isopropyl alcohol (IPA) and ascorbic acid (AA) to absorb hydroxyl and superoxide radicals, respectively. Six milligrams of each scavenger were independently added to the reaction mixture to determine the contribution of these radicals to the tribocatalytic degradation process.
Total Organic Carbon (TOC) Analysis: TOC measurements of the treated dye solutions were conducted using an Elementar Vario Select TOC analyzer (Langenselbold, Germany) with a high-temperature (850 °C) catalytic oxidation method. Each sample was measured three times to determine the standard deviation.

4. Conclusions

The degradation of the tetracycline antibiotic doxycycline was successfully achieved using ZnO and ZnO/Ce powders under varying magnetic stirring speeds (100, 300, and 500 rpm) in dark conditions. The increase in rotational speed significantly enhanced the degradation rate, demonstrating that the mechanical energy generated through friction effectively excites the electrons and holes in the ZnO and ZnO/Ce catalysts. This study highlights the potential of tribocatalysis as a sustainable and energy-efficient approach for the degradation of environmental pollutants, utilizing mechanical energy from the surrounding environment to drive the breakdown of harmful substances. The findings open up new possibilities for applying tribocatalysis in environmental remediation, offering a novel pathway to reduce the impact of pharmaceutical contaminants on ecosystems.

Author Contributions

Conceptualization, N.K.; methodology, N.K.; formal analysis, N.K.; investigation, D.I., H.K. and B.I.S.; data curation, N.K.; writing—original draft preparation, N.K.; writing—review and editing, N.K. and B.I.S.; visualization, D.I., N.K., H.K. and B.I.S.; supervision, N.K. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Data Availability Statement

Data are contained within the article.

Acknowledgments

Research equipment of distributed research infrastructure INFRAMAT, supported by the Bulgarian Ministry of Education and Science under contract D01-284/17.12.2019, was used.

Conflicts of Interest

The authors declare no conflicts of interest.

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Inorganics 12 00244 g001
Figure 1. XRD patterns of ZnO and ZnO/Ce powders.
Figure 1. XRD patterns of ZnO and ZnO/Ce powders.
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Figure 2. SEM images of (a) pure and (b) Ce-modified ZnO powders.
Figure 2. SEM images of (a) pure and (b) Ce-modified ZnO powders.
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Figure 3. (a) EDS spectra of ZnO powder modified with cerium ions (2 mol%); (b) mapping surface data for ZnO/Ce powder.
Figure 3. (a) EDS spectra of ZnO powder modified with cerium ions (2 mol%); (b) mapping surface data for ZnO/Ce powder.
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Figure 4. TEM micrographs of ZnO/Ce powder at (a) low and (b) high magnification.
Figure 4. TEM micrographs of ZnO/Ce powder at (a) low and (b) high magnification.
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Figure 5. XPS spectra of ZnO and Ce-modified ZnO powders showing (a) Zn 2p region in pure ZnO; (b) O 1s region in pure ZnO; (c) Zn 2p region in ZnO/Ce; (d) O 1s region in ZnO/Ce; (e) Ce 3d region in ZnO/Ce.
Figure 5. XPS spectra of ZnO and Ce-modified ZnO powders showing (a) Zn 2p region in pure ZnO; (b) O 1s region in pure ZnO; (c) Zn 2p region in ZnO/Ce; (d) O 1s region in ZnO/Ce; (e) Ce 3d region in ZnO/Ce.
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Figure 6. Raman spectra of pristine ZnO and ZnO/Ce powders.
Figure 6. Raman spectra of pristine ZnO and ZnO/Ce powders.
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Figure 7. (a) Decomposition of antibiotic via ZnO and ZnO/Ce powder using magnetic stirring 300 rpm; (b) kinetic fitting.
Figure 7. (a) Decomposition of antibiotic via ZnO and ZnO/Ce powder using magnetic stirring 300 rpm; (b) kinetic fitting.
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Figure 8. Possible reaction mechanism diagram for the tribocatalytic effect.
Figure 8. Possible reaction mechanism diagram for the tribocatalytic effect.
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Figure 9. Effect of scavengers on doxycycline degradation in tribocatalysis process using ZnO and ZnO/Ce powders.
Figure 9. Effect of scavengers on doxycycline degradation in tribocatalysis process using ZnO and ZnO/Ce powders.
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Figure 10. (a) Degradation of doxycycline at different rotation speeds, (b) relation between rate constants and different magnetic stirring speeds using ZnO and ZnO/Ce powders.
Figure 10. (a) Degradation of doxycycline at different rotation speeds, (b) relation between rate constants and different magnetic stirring speeds using ZnO and ZnO/Ce powders.
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Figure 11. UV/vis spectra showing DC tribodegradation over 24 h, with measurements taken every 6 h and rotation speed at 500 rpm, using (a) ZnO and (b) ZnO/Ce. The drug absorbance peak at 275 nm (λmax) is labeled.
Figure 11. UV/vis spectra showing DC tribodegradation over 24 h, with measurements taken every 6 h and rotation speed at 500 rpm, using (a) ZnO and (b) ZnO/Ce. The drug absorbance peak at 275 nm (λmax) is labeled.
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Figure 12. Histograms of TOC conversion.
Figure 12. Histograms of TOC conversion.
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Table 1. The values of rate constants and percent of doxycycline decomposition using the tribocatalytic process.
Table 1. The values of rate constants and percent of doxycycline decomposition using the tribocatalytic process.
Sample Powders100 rpm300 rpm500 rpm
k, h−1D, %k, h−1D, %k, h−1D, %
ZnO0.0296490.0483670.072580
ZnO/Ce0.0119240.0168300.035255
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Ivanova, D.; Kolev, H.; Stefanov, B.I.; Kaneva, N. ZnO and ZnO/Ce Powders as Tribocatalysts for Removal of Tetracycline Antibiotic. Inorganics 2024, 12, 244. https://doi.org/10.3390/inorganics12090244

AMA Style

Ivanova D, Kolev H, Stefanov BI, Kaneva N. ZnO and ZnO/Ce Powders as Tribocatalysts for Removal of Tetracycline Antibiotic. Inorganics. 2024; 12(9):244. https://doi.org/10.3390/inorganics12090244

Chicago/Turabian Style

Ivanova, Dobrina, Hristo Kolev, Bozhidar I. Stefanov, and Nina Kaneva. 2024. "ZnO and ZnO/Ce Powders as Tribocatalysts for Removal of Tetracycline Antibiotic" Inorganics 12, no. 9: 244. https://doi.org/10.3390/inorganics12090244

APA Style

Ivanova, D., Kolev, H., Stefanov, B. I., & Kaneva, N. (2024). ZnO and ZnO/Ce Powders as Tribocatalysts for Removal of Tetracycline Antibiotic. Inorganics, 12(9), 244. https://doi.org/10.3390/inorganics12090244

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