Open Access Article
Harry Lik Hock Laua,
Rusydi R. Sofiana,
Syahirah Nabilah Aedy Aewandy
a,
Nur Diana Bazilah Awang Idrisa,
Nur Aisyah Abdul Munira,
Nur Nabaahah Roslana,
Hussein Tahab,
Muhammad Nurc and
Anwar Usman
*a
aDepartment of Chemistry, Faculty of Science, Universiti Brunei Darussalam, Jalan Tungku Link, Gadong BE1410, Brunei Darussalam. E-mail: anwar.usman@ubd.edu.bn
bEnvironmental and Life Sciences, Faculty of Science, Universiti Brunei Darussalam, Jalan Tungku Link, Gadong BE1410, Brunei Darussalam
cCenter for Plasma Research, Integrated Laboratory, Universitas Diponegoro, Tembalang Campus, Semarang 50275, Indonesia
First published on 13th March 2026
The photocatalytic degradation of ibuprofen (IBU) in aqueous solution using titanium dioxide nanoparticles (TiO2 NPs) as a photocatalyst activated by 365 nm UV light irradiation was systematically investigated. The degradation of IBU was monitored by absorption spectroscopy, and the resulting overlapping spectra were deconvoluted to determine the concentrations of residual IBU and its photocatalytic degradation products. Effective immobilization and strong affinity of IBU for the photocatalyst surfaces were evidenced by the maximum adsorption capacity of 126 ± 4 mg g−1 on TiO2 NPs. Liquid chromatography-mass spectrometry and Fourier-transform infrared spectroscopy revealed that the stable photocatalytic degradation products were 1-(4-isobutylphenyl)ethanol, 4-isobutylbenzaldehyde, and 4-isobutyl-1-ethylbenzene, rather than complete mineralization to carbon dioxide and water. The degradation pathways were proposed to involve hydroxyl radical (OH˙) attack on the carboxylic group of IBU, leading to the formation of short-lived intermediates, followed by decarboxylation, hydroxylation, and demethylation reactions. The photocatalytic degradation was endothermic and spontaneous, accompanied by an increase in disorder. Based on the simplified Langmuir–Hinshelwood model, the observed degradation rate constant was 1.31 ± 0.02 × 10−2 min−1, primarily governed by mass transfer from the bulk solution to the photocatalyst surfaces. Toxicity assessments indicated that the photocatalytic degradation products of IBU are less toxic toward Artemia salina larvae, suggesting a reduced toxicity risk to microorganisms in the environment.
One of the NSAIDs frequently detected in aquatic environments is ibuprofen (IBU; 2-(4-isobutylphenyl)propionic acid), which is widely used as an analgesic, antipyretic, and anti-inflammatory agent for the treatment of inflammatory diseases, pain, fever, rheumatoid disorders, dysmenorrhea, and osteoarthritis.7 Global prescriptions of IBU exceed 20 million administrations annually, and nearly 15% of the administered dose is excreted as the unchanged parent compound. Actual usage is likely much higher due to its widespread availability as an over-the-counter medication. Consequently, IBU concentrations in wastewater effluents range from several nanograms per liter to a few tens of milligrams per liter.8 Because conventional sewage treatment plants are generally unable to completely remove pharmaceutical compounds, IBU is frequently detected in surface waters and poses potential risks to human health and aquatic ecosystems.9,10 Both in vivo and in vitro studies have revealed that long-term exposure to IBU is associated with elevated oxidative cellular stress, genotoxic and cytotoxic effects, as well as abnormal growth, reproduction suppression, and behavioral alterations in Dreissena polymorpha (zebra mussel).11
As IBU is non-biodegradable in nature, the development and implementation of effective methods for its removal from wastewater are indispensable. Adsorption has been widely explored for the removal of IBU from wastewater using various adsorbents, such as activated carbon,12 biochar,13 chitosan,14 and silica nanocomposites.15 Although adsorption can achieve high removal efficiency, secondary pollution arising from the lack of proper post-adsorption treatment of spent adsorbents remains a critical concern.2 On the other hand, various advanced oxidation processes (AOPs), including UV/H2O2 treatment,16 ozonation,17 the photo-Fenton process,18 and photocatalysis,19–21 have been applied to generate reactive oxygen species to oxidize and degrade IBU.22 Several studies have reported IBU degradation without definitive evidence, whereas photocatalysis studies clearly revealed the formation of 1-(4-isobutylphenyl)ethanol.19,21 This observation suggests that the aromatic ring of IBU remains intact and that, unexpectedly, IBU does not undergo complete mineralization under AOP treatments. The heterogeneous photocatalytic degradation processes and pathways of IBU have been scarcely reported, with only a few studies by Miranda et al.,19 Khendra et al.,20 and Jallouli et al.21 In these earlier works, the feasibility and efficiency of photocatalytic degradation of IBU using TiO2 under UV irradiation were evaluated, and the existence of 1-(4-isobutylphenyl)ethanol along with related transformation products were identified. However, comprehensive studies on the kinetics, mechanisms, and thermodynamics of IBU photocatalytic degradation have not yet been evaluated, most likely due to the significant overlap between the absorption spectra of IBU and those of its photocatalytic degradation products.23 Moreover, a quantitative comparison of the photocatalytic degradation behavior of IBU with those of other drugs, as well as an evaluation of the toxicity of degradation products of IBU, remains a research gap.
Therefore, the present work aims to investigate the detailed photocatalytic degradation of IBU on anatase titanium dioxide nanoparticles (TiO2 NPs) activated under UV light irradiation. Since the pioneering experiment investigating electrochemical photolysis of water on a TiO2 electrode in 1972 by Fujishima and Honda,24 TiO2 NPs have been widely utilized as photocatalysts. Their chemical stability, non-toxicity, cost effectiveness, and high photoactivity for generating O2˙− and OH˙ radicals make TiO2 NPs activated under UV light irradiation suitable for the photocatalytic degradation of a broad spectrum of organic pollutants, including synthetic dyes, pharmaceuticals, pesticides, phenolic compounds, and endocrine-disrupting chemicals in water matrices. To overcome the limitations associated with UV light irradiation, extensive efforts have been devoted to modifying TiO2 through metal and non-metal doping, as well as coupling with organic semiconductors. In particular, 6,13-pentacenequinone/TiO2 organo–inorganic nanocomposite has been reported to exhibit superior photoactivity under solar and visible light irradiation.25
In this study, the overlapping absorption spectra were carefully deconvoluted to determine the concentrations of IBU and its photocatalytic degradation products. The effects of various experimental parameters, including the initial IBU concentration, TiO2 NP dosage, pH of the medium, temperature, and the addition of hydrogen peroxide (H2O2), on the photocatalytic degradation of the NSAID were systematically examined. The objectives of this study are to elucidate the degradation kinetics, rate-limiting steps, and thermodynamic parameters by fitting the experimental data to the Langmuir–Hinshelwood (L–H), Weber–Morris (W–M) intraparticle diffusion, Arrhenius, and Eyring models. The photocatalytic degradation pathways of IBU were interpreted based on degradation products identified using liquid chromatography-mass spectrometry (LC-MS) and Fourier-transform infrared (FTIR) spectroscopy. Finally, the antibacterial activity and brine shrimp lethality of the degradation products were evaluated using the standard screening methods to assess their potential environmental risks. Overall, this study provides a comprehensive understanding of the photocatalytic degradation kinetics, mechanisms, thermodynamic parameters, and pathways of IBU. It also addresses existing knowledge gaps regarding its photocatalytic degradation behavior, and evaluates the environmental safety of the resulting degradation products.
Based on the absorption spectra of the IBU solutions, the absorbance was plotted as a function of the initial IBU concentration (C0), from which the molar extinction coefficient of IBU was estimated to be 254.74 ± 2.79 L mol−1 cm−1 at 262.5 nm (see Fig. S2), consistent with the range reported by Du et al.30 This value was subsequently used to determine the concentrations of the NSAID before and after the adsorption process using the Beer–Lambert law.
Each adsorption experiment was repeated in duplicate, and the average value was used in further analysis. The adsorption of IBU on the photocatalyst surfaces was quantified by the adsorption capacity (Qe), calculated as
| Qe = (C0 − Ce) × V/m | (1) |
The adsorption capacity of IBU on TiO2 NPs was measured at various C0 values, and the resulting isotherm data were fitted using the nonlinear equations of the Dubinin–Radushkevich, Elovich, Freundlich, Jovanović, Langmuir, and Temkin models. The basic theoretical concepts, mechanisms, and assumptions of each model have been reported in the literature.31–34 However, it is important to emphasize that photocatalysis occurs on the surface of a photocatalyst activated by light irradiation; therefore, the immobilization of IBU is expected to form only a single monolayer before being oxidized by the generated reactive oxygen species, consistent with the Langmuir isotherm model;29
| Qe = QmKLCe/(1 + KLCe) | (2) |
It should be noted that the use of high IBU concentrations in adsorption, photolytic, and photocatalytic experiments, exceeding those reported in surface water and groundwater (ng–mg L−1 range)8 is primarily for analytical purposes. In particular, with the relatively low molar extinction coefficient of 254.74 L mol−1 cm−1 such high IBU concentrations are required to obtain quantifiable absorption spectral changes, allowing more accurate determination of IBU concentrations and, consequently, more reliable insights into the degradation mechanisms, kinetics, and rate-limiting steps. In real wastewater matrices, although the presence of inorganic ions and natural organic matters may compete for reactive species and affect photocatalytic degradation efficiency of IBU, the intrinsic kinetic rate constants, rate-limiting steps, degradation pathways, and dominant reactive species are expected to remain unchanged.36 Therefore, in general, the photocatalytic degradation behavior of IBU can be extrapolated across different concentration scales.
The photocatalytic degradation of IBU was further evaluated at an irradiation time of 100 minutes under various photocatalyst dosages ranging from 2.5 mg to 15 mg, pH levels of the medium in the range of 4–10, adjusted by adding a few drops of 0.1 M HCl or 0.1 M NaOH into the IBU solution containing TiO2 NPs before irradiation, and temperatures ranging from 15 to 40 °C.
In addition, the reactive oxygen species (ROS) responsible for the photocatalytic degradation of IBU were identified by monitoring its degradation in the presence of TiO2 NPs after the addition of small amounts of either t-BuOH or p-BQ, which scavenge for OH˙ and O2˙− radicals, respectively. The effect of additional H2O2 on the photocatalytic degradation of IBU was also assessed by adding a small amount of the oxidizing agent. Each photocatalytic experiment was performed in duplicate, and the average value was used for analysis.
| Ct = C0 e−kpt + C | (3) |
On the other hand, the photocatalytic degradation kinetics and rate of IBU were deduced by fitting the experimental data to the L–H kinetic model;28,35,37,38
| dC/dt = kobsKLC/(1 + KLC) | (4) |
Temperature-dependent photocatalytic degradation kinetics were analyzed using the Eyring and Arrhenius equations, given respectively as29,39
| kobs = (kBT/h)e−ΔG/RT | (5) |
| kobs = A e−Ea/RT | (6) |
| kobs = (kBT/h)e−ΔH/RT+ΔS/R | (7) |
kobs and R
ln(hkobs/kBT) as functions of T−1.
All curve-fitting analyses were carried out using Origin 6.0 software.
LC-MS analysis was performed using a Nexera LC-40 XS Modular HPLC system (Shimadzu, Kyoto, Japan) with a 150 × 2.1 mm column. The mobile phase was 0.1% (v/v) acetic acid in water, with an injection volume of 20 µL and a flow rate of 0.2 mL min−1.
Separation of the photocatalytic degradation products was achieved using a binary solvent gradient, increasing from 2% to 50% and then to 98% at 5 and 10 minutes, respectively. Electrospray ionization was applied in both negative and positive modes at a temperature of 400 °C. Nitrogen gas was utilized as both the drying and nebulizing gas at a flow rate of 5 L min−1, with a drying temperature of 300 °C. Mass spectra were acquired over the m/z range of 50–2000 with a scan time of 0.1 s.35
FTIR analysis of the photocatalytic degradation products of IBU was performed using the KBr pellet method. The FTIR spectra were scanned in the range of 4000–400 cm−1 using a Spirit FTIR spectrometer (Shimadzu, Japan). The FTIR spectrum of IBU before photocatalysis was also measured for comparison. Based on the LC-MS and FTIR results, the chemical structures were constructed using ChemSketch, and were further confirmed by comparison with known compounds in the ChemSpider database.35
The toxicity of the photocatalytic degradation products of IBU was assessed using a brine shrimp (Artemia nauplii) lethality bioassay in a 12-well plate.40 Brine shrimp eggs were purchased from a local supplier and hatched at room temperature for 48 hours in artificial seawater prepared from water solution of commercial sea salt. Ten brine shrimps were transferred into each well, followed by the addition of 0.5 mL (200, 20, 2, 0.2 mg L−1) of the solution of photocatalytic degradation products of IBU and 3.5 ml of artificial seawater, resulting in an approximate final concentration of 25, 2.5, 0.25, and 0.025 µg L−1 per well. The plates were then incubated at room temperature overnight, and the number of surviving brine shrimps were counted in the following day. Toxicity was expressed as the 50% lethal concentration (LC50), defined as the concentration at which 50% of the brine shrimp population per well lethally affected.
The adsorption isotherm data of IBU on TiO2 NPs simulated using the nonlinear equations of the Dubinin–Radushkevich, Elovich, Freundlich, Jovanović, Langmuir, and Temkin models are shown in Fig. S3. Since all these isotherm models have the same levels of parameters, a direct comparison of their R2 and χ2 values was used to assess the suitability and accuracy of each model in fitting the experimental data. Based on these criteria, as summarized in Table S1, the adsorption isotherm of IBU was best described by the Langmuir model, which exhibited the highest R2 (0.997) and lowest χ2 (0.475). The suitability of the Langmuir model also supports the application of the L–H kinetic model in analyzing the photocatalytic degradation process.
The best fit of the Langmuir isotherm model revealed the maximum adsorption capacity (Qm) of 126 ± 4 mg g−1 (or equivalent to 0.612 ± 0.018 mmol g−1) and a Langmuir isotherm constant (KL) of 5.40 ± 0.7 ×10−4 L mg−1. These findings suggest high immobilization and efficient adsorption of IBU on TiO2 NPs, which is significantly higher than that reported on chitosan (24.21 mg g−1)14 and slightly lower than that of activated carbon derived from sisal waste via chemical activation with K2CO3 (145.2 mg g−1).12 This behavior is due most likely to the strong affinity of the carboxylic acid group of IBU toward the oxygen atoms on the surfaces of TiO2 NPs. This interpretation is further supported by the relatively low KL value, which suggests that a high IBU concentration is required to reach adsorption–desorption equilibrium.
For direct photolysis, as shown in Fig. S4(A), IBU exhibits no changes in absorbance under 365 nm light irradiation, even after prolonged exposure times of up to 180 minutes. The fine-structured absorption spectrum, which arises from vibronic transitions, also remains unchanged. The results suggest that the chemical and conformational structure of IBU remains entirely intact, as this analgesic compound is not effectively excited by 365-nm light photons. In other words, IBU undergoes negligible degradation via direct photolysis. The addition of H2O2 also did not result in observable degradation of IBU by the photolysis, emphasizing that direct oxidation of IBU by H2O2 or by OH˙ radicals generated through photodissociation of the oxidizing agent in solution is negligible. Such inefficient oxidation by UV/H2O2 treatment is not unexpected, as the photodissociation efficiency of H2O2 in solution under UV irradiation at wavelengths longer than 250 nm is very low.
Nevertheless, the degradation kinetics and rate of IBU by the direct photolysis were analyzed. Referring to the first-order kinetic model, given in eqn (2), the relative concentration (Ct/C0) of IBU was plotted as a function of irradiation time, t, and was simulated using a single-exponential decay, as shown in Fig. S4(B). The best fit yielded the kp value of 3.27 × 10−3 min−1 with degradation efficiency being less than 2% after 180 minutes of irradiation. Under the same experimental conditions, the degradation kinetics and rate of IBU are significantly lower than those reported for rifampicin and cephalexin antibiotics, where the kp values are 1.67 × 10−2 min−1 28 and 1.85 × 10−2 min−1 29 with efficiencies being about 7.2% and 3.0%, respectively. These results further confirm that IBU is considerably more resistant to direct photolytic degradation than these antibiotics.
The kinetics of photocatalytic degradation of IBU was subsequently analyzed using the L–H model (eqn (4)). Given that the KL value for IBU adsorption on TiO2 NPs is on the order of 10−4 L mg−1 and C0 of IBU is 200 mg L−1, the condition KLC << 1 is satisfied. Under this condition, integration of eqn (4) analytically lead to the simplified L–H kinetic model;37,38
| Ct = C0e−kobst + Cec | (8) |
From the best global fitting of eqn (8) to the kinetic data for IBU degradation, as shown in Fig. 1(c), the kobs value was estimated to be 1.31 ± 0.02 ×10−2 min−1. This value is slightly lower than those for the overall photocatalytic degradation of cephalexin (2.30 × 10−2 min−1) and rifampicin (1.63 × 10−2 min−1) on TiO2 NPs under the same experimental conditions.28,29 Given that the typical coverage coefficients of these pharmaceutical compounds on TiO2 NPs are comparable, within the range of 1.5 × 10−3 to 1.8 × 10−3 L mg−1, the photoreaction coefficient of IBU, which is linearly related to the rate constant of the photocatalytic degradation, was lower than those of cephalexin and rifampicin. This indicates that IBU is significantly more resistant to photocatalytic degradation than these antibiotics. A plausible explanation for the lower photoreaction coefficient of IBU is the limited reactive radicals that are capable to oxidize this analgesic compound.
As shown in Fig. 1(c), the photocatalytic degradation rate is essentially high. The degradation efficiency for 200 mg L−1 IBU using 2.5 mg TiO2 NPs was as high as 95%. In comparison, under the same experimental conditions, the photocatalytic degradation efficiency of 75 mg L−1 cephalexin using 2.5 mg TiO2 NPs was about 68%, while that of 50 mg L−1 rifampicin using 1.0 g TiO2 NPs was 87%. These findings emphasize that the intermediate species and degradation products resulting during the photocatalytic oxidation reaction of IBU by ROS generated on the surfaces of TiO2 NPs may rapidly escape from the solvent cage in the close vicinity of the photocatalyst surfaces.43 In this context, the relatively simple aromatic structure of IBU, as well as its photocatalytic degradation intermediates and products, are less steric hindrance than those of cephalexin and rifampicin. A similar interpretation has been pointed out in the higher, faster, and more efficient photocatalytic degradation rate of methylene blue, which is relatively more planar and less sterically hindered compared to rhodamine B and auramine O.38
It is important to emphasize that both the photocatalytic degradation of IBU and the formation of its degradation products proceed with the same rate constant while conserving the total concentration. This observation suggests that photocatalytic degradation largely conserves the aromatic ring of IBU, converting it into 1-(4-isobutylphenyl) derivatives, rather than being further mineralized into carbon dioxide and water. This behavior highlights the stable formation of recalcitrant degradation products which can repel further rapid oxidation by radical attacks. This interpretation is supported by the steady absorbance of UV-vis absorption spectrum of IBU upon photocatalysis at prolonged irradiation times.23 This behavior is in contrast to the more complex degradation pathways of IBU associated with persulfate- and hydroxylamine-based oxidation systems.44,45
The kinetics of photocatalytic degradation of IBU are generally governed by the diffusion and immobilization of the pharmaceutical compound on the photocatalyst surfaces. To verify this viewpoint, the kinetic data were analyzed using the Weber–Morris intraparticle diffusion model;46
| C0 − Ct = kit1/2 + Cl | (9) |
The effect of photocatalyst dosage on the photocatalytic degradation of IBU was investigated by monitoring the absorption spectra after 100 minutes of irradiation in the presence of different TiO2 dosages ranging from 2.5 to 15 mg, as shown in Fig. S6. The absorbance increased nonlinearly with increasing catalyst dosage. This trend suggests that the formation of photocatalytic degradation products of IBU increased with TiO2 dosage, and tends to saturate at higher photocatalyst dosages. Accordingly, the degradation efficiency of IBU is nonlinearly enhanced before reaching saturation. The spectra were then carefully deconvoluted, and the concentrations of IBU and its photocatalytic degradation products are presented in Fig. 2(a). It is clearly observed that, upon photocatalytic treatment with 15 mg TiO2 NPs, the initial IBU concentration of 200 mg L−1 decreased to nearly zero, with the compound being almost completely converted into its photocatalytic degradation products.
It is worth noting that the photocatalytic degradation behavior of pharmaceutical compounds is closely associated with the ROS generated during photocatalysis.22 In particular, with the standard reduction potential of conduction band typically around −0.28 V vs. NHE and that of valence band around +3.2 V vs. NHE, the photogenerated electron–hole pair of anatase TiO2 NPs that migrated to the photocatalyst surfaces readily react with solvated oxygen and water molecules to produce O2˙− and OH˙ radicals, respectively. To identify the responsible reactive species for the degradation process, photocatalytic degradation of IBU was investigated in the presence of radical scavengers. Fig. S7 shows the absorption spectra of IBU solutions before and after photocatalysis on TiO2 NPs in the presence of various concentrations of t-BuOH and p-BQ, which act as scavengers for OH˙ and O2˙− radicals, respectively, generated on the photocatalyst surfaces upon light excitation. The absorption spectra increasingly resembled that of pristine IBU upon the addition of higher concentrations of t-BuOH, whereas the spectra remained nearly unchanged upon the addition of p-BQ. Spectral deconvolution further confirmed that, as shown respectively in Fig. 2(b) and (c), the photocatalytic degradation of IBU was significantly suppressed in the presence of t-BuOH, while it was not noticeably affected by p-BQ. This scavengers study unambiguously indicates that the photocatalytic degradation of IBU on TiO2 NPs is solely due to oxidation reaction by OH˙ radicals. Since photocatalysts may also generate reactive singlet oxygen molecule (1O2), the photocatalytic degradation of IBU via singlet oxygen was further examined using rose bengal as photosensitizer under visible light irradiation. Since no changes in the absorption spectra were observed, even after prolonged irradiation times of up to 180 minutes, it can be concluded that IBU was hardly oxidized by singlet oxygen.
It is noteworthy that the photocatalytic degradation of various classes of antibiotics, including rifampicin and cephalexin, on TiO2 or SrTiO3 NPs can be achieved by both the generated OH˙ and O2˙− radicals (see Table S2). The dominant role of OH˙ radicals in the degradation of IBU can be rationalized from a redox (reduction–oxidation) perspective. Given the standard reduction potentials of ROS, including OH˙, SO4˙−, O2˙−, and 1O2 which are approximately +2.8 V, +2.6 V, +0.91 V, and +1.24 V vs. NHE, respectively, the overall results suggest that that the oxidation potential of IBU lies below +2.6 V but above +1.24 V vs. NHE. Consequently, the relatively high oxidation resistance of IBU necessitates ROS with high reduction potentials for its effective degradation. The high oxidation resistance of IBU is also supported by previous observations of IBU degradation on BaTiO3 NPs via piezoelectric catalytic activation of persulfate, which continuously generates SO4˙− and OH˙ radicals. In this case, the comparable high standard reduction potentials of SO4˙− and OH˙ radicals were the reason for their contributions (approximately 53% and 44%, respectively) to the overall degradation of IBU.47 It is also interesting to note that, with the standard potential of the valence band of anatase TiO2 NPs being about +3.2 V vs. NHE, direct oxidation of IBU by photogenerated holes (h+) via electron abstraction is thermodynamically feasible. However, the contribution of hole direct oxidation is likely minor under these conditions, as this process requires the immobilization of IBU on the photocatalyst surfaces. In contrast, the oxidation of surface-adsorbed water molecules by holes to generate OH˙ radicals is more competitive and thus dominates the photocatalytic degradation of IBU.
Considering the critical role of OH˙ radicals in the photocatalytic degradation of IBU on TiO2 NPs, further evidence can be obtained by the addition of H2O2, which accelerates the generation of OH˙ radicals. The effect of varying amounts of added H2O2 on the photocatalytic degradation of an initial IBU concentration of 200 mg L−1 (0.97 mM) is reflected by the absorption spectra shown in Fig. S8. Based on spectral deconvolution, the extent of IBU degradation increased nonlinearly from 0.69 mM in the absence of H2O2 to 0.88, 0.93, and 0.96 mM in the presence of additional 0.001%, 0.005%, and 0.010% v/v H2O2 in 20 mL solution of IBU, as shown in Fig. 2(d). Notably, the initial 0.97 mM IBU was almost completely degraded and converted into degradation products after 100 minutes of photocatalysis using 2.5 mg TiO2 NPs in the presence of 0.010% v/v H2O2. The results demonstrate enhanced photocatalytic degradation of IBU upon the addition of a small amount of H2O2, which may arise from either the UV light-induced photodissociation of H2O2 to generate additional OH˙ radicals in the solution,48 or scavenging of photogenerated electrons on the photocatalyst surfaces.49 However, considering that the diffusion coefficient of IBU is 5 × 10−10 m2 s−1, and the lifetime of OH˙ is about 20 ns, during which IBU diffuses only within 10 nm2, the oxidation reaction of IBU in the solution should be less pronounced. Therefore, the enhancement effect of H2O2 on the photocatalytic degradation of IBU is more likely attributable to photogenerated electron scavenging, which suppress electron–hole recombination and accelerates OH˙ radical formation on the photocatalyst surfaces.50 The increased degradation rate of IBU on TiO2 NPs in the presence of H2O2 provides further evidence for the crucial role of OH˙ radicals in the photocatalytic process.
It is well known that IBU exhibits acidic characteristic with a pKa of 4.91, which is related to its pharmacological action in inhibiting enzymes responsible for inflammation, pain, and fever.51 IBU undergoes a transition from its neutral to an anionic form at pH 4.91 due to protonation and deprotonation of the carboxylic group. Therefore, the pH of the medium is an important factor determining the photocatalytic degradation of IBU. The ambient pH of IBU solution was fairly neutral, while acidic and alkaline conditions were adjusted by adding a few drops of 0.1 M HCl or 0.1 M NaOH, respectively. As shown in Fig. S9(a), before photocatalysis, IBU solutions in the pH range of 4–10 exhibited similar absorption spectral features, although the absorbance increased with pH of the medium. This observation suggests that the conformational structure of IBU remains intact across this pH range, while the oscillator strength of IBU anion increases due to higher electron delocalization. Nevertheless, changes in the ionic state strongly affect the immobilization, electrostatic interactions, and photocatalytic degradation rate of IBU on the surfaces of TiO2 NPs.52 Therefore, pH of medium is a crucial parameter governing the photocatalytic degradation behavior of IBU.
The absorption spectra of IBU after photocatalysis at different pH values are shown in Fig. S9(b), highlighting that the residual absorbance of IBU after photocatalysis depends strongly on the pH of the medium. Since no significant changes in the spectral feature were observed, it is reasonable to conclude that IBU degradation proceeds via similar pathways across the investigated pH range, while the increase in absorbance reflects a lower photocatalytic degradation rate of IBU. Spectral deconvolution confirmed that the photocatalytic degradation rate of IBU decreased sharply from pH 4 to 5, followed by a nearly linear decrease with increasing pH, as shown in Fig. 3(a). The results straightforwardly indicate that the photoreaction coefficient of protonated IBU is higher than that of its deprotonated form, and that photocatalytic degradation is more efficient under acidic conditions than under alkaline conditions. This finding can be attributed to the point of zero charge of TiO2 NPs (pH 6.1),53 above which electrostatic interactions between anionic IBU and the negatively charged surface of the photocatalyst is inefficient, consequently diminishing the affinity of the negatively charged IBU toward the photocatalyst.
As the photocatalytic degradation kinetics of IBU are governed by its temperature-dependent diffusion from the solution to the surfaces of TiO2 NPs, thermodynamic parameters were further elucidated based on the degradation behavior of IBU at different temperatures. Fig. S10 shows representative absorption spectra of IBU before and after photocatalysis, revealing higher absorbance changes at higher temperatures. This observation indicates that the photocatalytic degradation of IBU is accelerated at higher temperatures, most likely due to higher kinetic energy and mobility of IBU molecules in solution. These factors enhance the immobilization of the pharmaceutical compound onto the photocatalyst surfaces, thereby accelerating its photocatalytic degradation kinetics. The temperature-dependent kobs value is presented in Fig. 3(b), and was used to estimate the thermodynamic parameters of the photocatalytic degradation of IBU using the Arrhenius and Eyring equations.
From the linear plot of ln
kobs versus T−1 shown in Fig. 3(c), the Ea value for the photocatalytic degradation of IBU was found to be 18.84 ± 0.56 kJ mol−1, much higher than those reported for rifampicin (1.585 ± 0.079 kJ mol−1) and cephalexin (3.949 ± 0.257 kJ mol−1). The values of ΔH and ΔS were obtained from the slope and y-intercept of the linear plot of R
ln(hkobs/kBT) versus T−1, as shown in Fig. 3(d), to be 0.016 ± 0.001 kJ mol−1 and 0.161 ± 0.003 J mol−1 K−1, respectively. Using these parameters, the ΔG values were calculated to be in the range from −0.030 to −0.034 kJ mol−1. These thermodynamic parameters of photocatalytic degradation of IBU are summarized in Table S3. The positive values of ΔH and ΔS indicate that the photocatalytic degradation of IBU is weakly endothermic and thermodynamically favorable, and is accompanied by an increase in disorder at the photocatalyst surfaces. The negative ΔG values further suggest that the photocatalytic degradation proceeds spontaneously on the surfaces of TiO2 NPs under UV light irradiation.
The chemical structures of IBU degradation products, P1–P3, were confirmed by FTIR spectroscopy. The FTIR spectra of IBU before and after photocatalytic degradation, as shown in Fig. 4, exhibit significant differences. The FTIR spectrum of IBU displays several intense bands at 3503 and 3349 cm−1, which are assigned to the asymmetric and symmetric OH stretching vibrations of the carboxylic acid group. The bands observed at 2956, 2917, and 2867 cm−1 are due to the C–H bond in the benzene ring, methyl groups, and ethylene moiety, respectively. The band at 1704 cm−1 is due to the C
O stretching vibration. Bands at 1548, 1411, and 1119 cm−1 are attributed to the stretching vibrations of C
C in the benzene ring, C–C in aliphatic moieties, and C–O in the carboxylic group, respectively. The bands at 1293 and 1056 cm−1 are assigned to C–H vibrations, while those at 889, 845, 785, and 587 cm−1 arise from rocking and out-of-plane bending vibrations of C–H groups. Finally, the peaks at 749 and 494 cm−1 are attributed to skeletal vibrations.55,56
The FTIR spectra of IBU after degradation exhibit several bands that can be assigned to the presence of a small amount of residual IBU. Several prominent new bands are observed, particularly the two broad bands with peaks at 1548 and 1411 cm−1, which confirm the C
C stretching vibrations in the benzene ring and the C–C stretching vibrations in the aliphatic moieties of P1–P3, respectively. The relatively unchanged vibrational bands at 587 and 494 cm−1 indicate that the out-of-plane C–H bending vibrations and skeletal vibrations remained unchanged. Therefore, FTIR spectral analysis confirms the chemical structures of the photocatalytic degradation products, P1–P3, which remain stable without further breakdown or complete mineralization, as proposed on the basis of LC-MS measurements. Nevertheless, further inorganic carbon analysis may be further needed to assess mineralization and minor products.
Based on the proposed photocatalytic degradation pathways, the observable overall rate constant, kobs, depends on the relative magnitudes of k + k' compared with k1 + k2 + k3. The reaction of IBU with OH˙ radicals, which is controlled by diffusion of the NSAID to the photocatalyst surfaces, is much slower than that of the following decarboxylation, hydroxylation, demethylation, and hydrogenation reactions. Therefore, it is reasonable to assume that kobs value reflects the diffusion of IBU to the photocatalyst surfaces and is proportional to the diffusion-limited reaction rate constant. Consequently, kobs is related to the diffusion coefficient and the encounter distance of IBU and the photocatalyst surfaces, as described by the general Smoluchowski equation.57
Based on triplicate experiments conducted at concentrations of 200, 20, 2, and 2 mg L−1, as summarized in Table 1, a total of 120 A. salina shrimp larvae were tested, and the average larval mortalities were in the range from 0 to 50%. Larval mortality increased nonlinearly with increasing IBU concentration, with the lethality concentration (LC50) approximately 175 mg L−1, confirming that IBU exhibits moderate toxicity. After photocatalytic treatment, the larval mortality decreased significantly with increasing irradiation time, suggesting that the photocatalytic degradation products of IBU possess higher LC50 values. For example, the LC50 of IBU after 100 minutes of irradiation exceeded 1000 mg L−1, strongly suggesting that the degradation products (P1–P3) may be non-toxic to A. salina shrimp under laboratory conditions. These results may indicate that the persistent photocatalytic degradation products of IBU are unlikely to pose significant toxicity risks to microorganisms in the environment. However, isolation of individual IBU degradation products and comprehensive toxicity evaluations, including animal testing, dose–response assessments, and other chemical risk analyses should be conducted in further detail to provide a clearer understanding of their toxicological effects and to more accurately determine the environmental safety of the resulting persistent degradation products.
| Concentration (mg L−1) | Irradiation time [min] | Mortality (%) | |
|---|---|---|---|
| IBU | 200 | 0 | 50 |
| 20 | 17 | ||
| 2 | 10 | ||
| 0.2 | 0 | ||
| 200 | 10 | 27 | |
| 20 | 10 | ||
| 2 | 7 | ||
| 0.2 | 0 | ||
| 200 | 50 | 20 | |
| 20 | 7 | ||
| 2 | 3 | ||
| 0.2 | 0 | ||
| 200 | 100 | 10 | |
| 20 | 3 | ||
| 2 | 0 | ||
| 0.2 | 0 |
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