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Oxone activated TiO2 in presence of UV-LED light for the degradation of moxifloxacin: A mechanistic study
⁎Corresponding authors. majid.chemist@yahoo.com (Majid Muneer), bosalvee@yahoo.com (Munawar Iqbal)
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Received: ,
Accepted: ,
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.
Peer review under responsibility of King Saud University.
Abstract
This work provides new insight into the development of the TiO2/Oxone/UV-LED process for organic contaminant degradation as well as hospital waste management. The Moxifloxacin (MOX) degradation using Oxone activated TiO2 under UV-LED was studied. The TiO2/Oxone/UV LED process was carried out by the addition of Oxone (0.025, 0.05, 0.1 and 0.2 mM) activated by TiO2 different concentrations 0.0125, 0.025, 0.05, 0.1 and 0.5 g/L. The degradation efficiency was studied by HPLC having UV/Vis detector, C18 column (5µ, 4.6 × 250 mm2). The complete removal of 10 ppm of MOX occurred at 0.1 g/L TiO2 and 0.1 mM Oxone with UV-LED exposure time of 12 min. The TOC analysis was performed and 55% TOC reduction was observed at described procedure. The parameters such as drug initial concentration, Oxone, TiO2 dosages and pH were optimized and their effects on degradation were noted. The pseudo-first order reaction kinetics was observed for MOX degradation. It was revealed from the mechanism of activation that and have played a key role in the degradation. The effect of pH (3.6–11) was observed to evaluate the degradation rate of Moxifloxacin. The pH 9.4 achieved the maximum degradation. The UPLC-ESI-MS analysis was performed to identify the intermediates and degraded end-products.
Keywords
Moxifloxacin
Photocatalytic degradation
UV-LED
Advanced Oxidation Process
1 Introduction
The Moxifloxacin is a Fluoroquinolone (FQ) and is a broad-spectrum antibiotic and has been frequently utilized to cure infection (Sayed et al., 2015a; Sayed et al., 2015b; Kümmerer, 2009; Speltini et al., 2010). The minute amount of this antibiotic affects the aquatic bodies badly when get mixed in any water body (Robinson et al., 2005; Celiz et al., 2009; Jjemba, 2006; Petrovic et al., 2003). The pharmaceutical based wastewater requires treatment prior to its discharge. The routine treatment methods have been applied to treat, but these exhibited a less performance for the removal of the pollutants (Adu et al., 2020; Jamil et al., 2020; Sohail et al., 2020). The methods such as filtration, coagulation, chlorination, etc are technologically deficit to meet the complete degradation and transfer pollutants from one phase to other rather elimination (Nebot et al., 2015; Muneer, 2020; Kanjal et al., 2020; Alsager et al., 2018; Saeed et al., 2018; Basfer et al., 2018). The advanced oxidation processes (AOPs) are efficient and innovative for the treatment of antibiotics as well as other toxic compounds (Liu et al., 2014; Iqbal and Bhatti, 2015; Kanjal et al., 2020). These include O3/UV/H2O2, gamma/H2O2, UV/H2O2, UV/Fe2+/H2O2, and UV/TiO2 etc. are effective methods to degrade the organic matter present in the aquatic environment (Van Doorslaer et al., 2015, 2012, 2011; Paul et al., 2007; Muneer et al., 2020; Saeed et al., 2015; Muneer et al., 2012). Among AOPs, the TiO2 assisted photo-catalysis is an efficient option due to production of h+, OH•, e- and •O2– when exposed to UV light as shown in equation (1) (Yahya et al., 2017; Marugan et al., 2010; Izumi et al., 1981).
While, e- and h+ represent the electron and hole generated during photo-catalysis respectively (Jaeger and Bard, 1979; Kessler, 2013). The UV-LED lamps are eco-friendly than conventional UV lamps (Yoshihiko et al., 2014; Ibrahim et al., 2014; Crawford et al., 2005). However, the e- and h+ recombine and decrease the photo-catalysis efficiency. To fill this gap, the electron acceptors species such as hydrogen peroxide, persulfate, and Oxone were used during photocatalytic process (Liu et al., 2014). The use of Oxone as an electron acceptor is a better option in order to degrade the organic compounds via reactive radicals generation as shown in equation (2) (Moradi et al., 2014; Oh et al., 2016).
The Oxone activation by UV-LED can be achieved by transition metals or photo-catalysts such as TiO2 (Chen et al., 2012). In the established literature, a few studies were reported about the TiO2/Oxone/UV-LED process for the drug degradation. In the present study, the TiO2/Oxone/UV-LED was used to degrade the Moxifloxacin antibiotic. The degradation study and intermediate/end-product analysis was carried out by using the UPLC-ESI-MS.
2 Material and methods
2.1 Chemicals
The physicochemical properties of Moxifloxacin are shown in Table 1. The titanium dioxide (TiO2) was used as a catalyst and purchased from Degussa Company, Germany. The Acetonitrile and formic acid were used as mobile phases. While methanol (CH3OH), sodium thiosulfate (Na2S2O3), hydrochloric acid (HCl), sodium hydroxide (NaOH) and Oxone (2KHSO5.KHSO4.K2SO4) were procured from Sigma-Aldrich, USA.
Name of drug
Molecular formula
Molecular weight
λmax
Moxifloxacin
C21H24 FN3O4
401.438 g/mol
2.2 Experimental setup
The MOX solutions having concentrations 10 to 40 mg/L were prepared using ultra-pure water; photodegradation was performed in photo-reactor as described in Fig. 1. The UV-LED lamp having 100 W intensity, emitting 365 nm light with self-cooled chamber with agitation. A catalyst (TiO2) was mixed with 100 mL of drug (10 mg/L) solution and was placed in dark. The Oxone (oxidant) was then added and after predetermines time interval solution was utilized for further analysis. The UV-LED lamp was fixed vertically 8 cm above the solution.Experimental setup of UV chamber.
2.3 Analytical procedures
The decrease in MOX concentrations was monitored by HPLC, C18 column with UV/Vis detector. A mixture of Acetonitrile, water and phosphoric acid (20%, 80% and 0.1% respectively) was used as a mobile phase with flow rate of 1 mL/min while degassing was done prior to run. The Shimadzu TOC-L analyzer was used for TOC analysis. The intermediate were identified using UPLC-ESI-MS detector. The Tribrid Mass Spectrometer Orbitrap Fusion Lumos (Thermo Fisher Scientific, USA) and the UPLC Waters Acquity (Waters, USA) comprised with Acquity BEH C18 column (1.7 µm, 2.1 mm × 50 mm) was employed. The mobile phase used for intermediates detection was a mixture of acetonitrile and formic acid (100% and 0.1% respectively) with the flow rate of 0.3 mL/min.
3 Results and discussion
3.1 Degradation of MOX using UV-LED/TiO2/PMS
The performance of different processes such as TiO2/dark, Oxone/dark, TiO2/Oxone/dark, UV-LED, Oxone/UV-LED, TiO2/UV-LED and TiO2/Oxone/UV-LED was examined and then the MOX degradation efficiency was compared (Fig. 2). The obtained data showed 4% and 10% degradation for 10 ppm solution using the adsorption (TiO2/dark) and photolysis (UV-LED) respectively. The degradation was noted as 20% and 56% after Oxone/UV-LED and TiO2/UV-LED treatments respectively. The complete degradation was achieved after TiO2/Oxone along with UV-LED for 12 min exposure time. The degradation of MOX suggests the seminal role of Oxone (HSO5-) in capturing the generated h+ and may cause to produce excess sulfate and hydroxyl radicals as shown in Eqs. 3–6 (Zhang et al., 2015; Chen et al., 2007).
Degradation kinetics of MOX by using the oxidant along with catalyst.
The pseudo-first order kinetics was observed for data (Eq. (7)).
Where k and C indicate the reaction rate constant and concentrations of MOX at time t respectively. The slope of ln (C/C0) versus t gives the value of k and C0 represents the initial concentration of the drug.
3.2 Initial concentration influence on MOX degradation
The TiO2/Oxone/UV-LED process was used to check the effect of the initial MOX concentration on the photodegradation efficiency (Fig. 3) having concentrations 10–40 mg/L of drug. The degradation efficiency was reduced as the MOX concentration increased. This can be rationalized by the increase the number of targeted molecules, compete with a limited number of reactive species (•OH and
) and may decrease the rate of drug degradation due to competition among the molecules. Furthermore, the active sites of the catalyst become over occupied can render the production of •OH and O2•- (Tokode et al., 2012). The results are in accordance to the.Effect of drug concentration in presence of oxidant and catalyst.
findings of Van Doorslaer and his co-workers performed in the degradation of MOX by UV/TiO2 process (Van Doorslaer et al., 2011).
3.3 pH influence on MOX degradation
The pH of the media affects the photocatalytic activity (Hermann, 1999) and may alter the catalyst’s surface property and may influence the adsorption nature of the pollutant (Abdelhaleem and Chu, 2017; Hsiung et al., 2016; Natarajan et al., 2011; Ahn et al., 2016). The effect of change in pH from 3.6 to 11 using 0.1 mM Oxone and 0.1 g/L TiO2 using UV-LED light was examined (Fig. 4). The complete degradation at pH 9.4 while 80% and 90% in case of acidic and neutral media was observed respectively. In acidic and alkaline media, the TiO2 is positively and negatively charged respectively as shown in eqs. (9) & (10) (Langlois et al., 2005).
The effect of pH on MOX along with oxidant and catalyst.
In acidic condition, the H-bonding between hydrogen ion and O-O group in
reduces the positive charge on
and decreases the photodegradation by hindering the interaction of
with surface of catalyst (Liu et al., 2015; Guan et al., 2011). Furthermore, H+ can scavenge sulfate and hydroxyl radicals at low pH (pH 3 or below) based on equations 11–13 (Sun et al., 2012; Jaafarzadeh et al., 2017). The complete degradation was achieved in alkaline condition (at pH 9.4) which is due to increase in
formed due to adsorption of OH− on the surface of catalyst (Guan et al., 2011). This is also the optimum pH. Further increase in pH may reduce the process efficiency due to less adhesion of drug molecules on the surface of catalyst as a result of repulsion between TiO2 and MOX (Muruganandham and Swaminathan, 2004).
3.4 Catalyst dose influence on MOX degradation
The Fig. 5 shows the effect of catalyst dosage (0.0125–0.5 g/L) on the degradation efficiency of MOX. The complete degradation was achieved for 10 ppm drug aqueous solution by using UV-LED light in combination of oxidant and catalyst at UV-LED exposure time of 12 min. The availability of more active sites due to increased amount of catalyst enhanced the drug degradation. The degradation reduced suddenly when TiO2 was overdosed (0.5 g/L) due to the reduction in the penetration of light at higher catalyst dosages (Chu and Wong, 2004).Effect of TiO2 dosage on the degradation of MOX.
3.5 Oxidant influence on MOX degradation
During the photocatalysis, electrons and the holes may recombine, which result limited degradation. Electron acceptor such as oxone is added to the reaction system in order to overcome the recombination. The TiO2/UV-LED process have shown 55% degradation, which enhanced to 100% along with Oxone (0.2 mM) as shown in Fig. 6. The increase in MOX degradation efficiency can be justified by the production of reactive radicals through the Oxone decomposition by the photo-catalyst (Madhavan et al., 2006) as shown by the equations 14–16 (Dhanalakshmi et al., 2008).
Effect of Oxone on degradation efficiency along with catalyst.
3.6 Mineralization efficiency
The organic compounds could be more harmful to the environment as compared to parent compounds when degraded to smaller molecules via oxidation process. The mineralization was carried out by using total organic carbon (TOC) analysis (Zazouli et al., 2007). Fig. 7 shows the mineralization results of Moxifloxacin at different experimental conditions. During TiO2/Oxone/UV-LED process, about 55% of TOC reduction was observed while only 18% TOC removal was observed in case of Oxone/UV-LED process. The mineralization took place in the following order TiO2/Oxone/UV-LED > UV-LED/TiO2 > UV-LED/Oxone. The TOC reduction in the TiO2/Oxone/UV-LED process reveals that the process could be effective technique for the removal of the intermediates resulting from the photodegradation of Moxifloxacin.TOC measurements in UV-LED/TiO2/Oxone process.
3.7 Byproducts distribution
The proposed mechanism of MOX photocatalytic degradation by TiO2/Oxone/UV-LED process is shown in scheme 1. The ion [M + H+] where M is the molecular mass of the respective analyte generated because of a proton in order to get positively charged molecular ion in all analytes while Table 2 summarizes the intermediates’ information with structure. The MS spectra of MOX (m/z 402) yields ions at m/z 374 and 358 as a result of CO and CO2 loss, respectively. Whereas, the intermediate specie at m/z 321 identified with the loss of HF at m/z 341 (Chai et al., 2011). The proton-bound complex resulted complementary products at m/z 293 and 110 (Zhang et al., 2012) formed by the rearrangement of hydrogen (Hudson and McAdoo, 2007). Due to loss of CH3 and H2O, the ion with m/z 293 produced an ion at m/z 279 (Kingston et al., 1975). The fragment pathways for protonated moxifloxacin have shown conflict with the fragment pathways reported by (Raju et al., 2012). However, the elimination of neutral species such as CO, H2O and CO2 took place via same fragment pattern in both studies, while, a significant variation in relative abundance of the ions was observed.Proposed pathways of Moxifloxacin using UV-LED/TiO2/Oxone process.
Product ID
Molecular Ion [M + H+]
Proposed Structure
Inter-1
293
Inter-2
434
Inter-3
416
Inter-4
418
Inter-5
430
Inter-6
387
Inter-7
321
Inter-8
306
Inter-9
358
Inter-10
279
Inter-11
246
Inter-12
374
4 Conclusions
In this study, the performance of MOX degradation was assessed by using UV-LED/TiO2/Oxone process. The obtained data revealed that TiO2 had a catalytic activity for Oxone activation under the UV-LED light. A complete degradation of Moxifloxacin and 55% mineralization revealed the outstanding performance of TiO2/Oxone/UV-LED combined process for the removal of the intermediates. The TiO2/Oxone/UV-LED process could be implemented through the activation of Oxone as a sustainable and environmentally friendly approach to degrade of organic matter in aquatic environment.
Funding
This research was funded by Princess Nourah bint Abdulrahman University Researchers Supporting Project (Grant No. PNURSP2022R11), Princess Nourah bint Abdulrahman University, Riyadh, Saudi Arabia.
Acknowledgements
The authors express their gratitude to Princess Nourah bint Abdulrahman University Researchers Supporting Project (Grant No. PNURSP2022R11), Princess Nourah bint Abdulrahman University, Riyadh, Saudi Arabia.
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
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