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Study on the behavior and mechanism of NiFe-LDHs used for the degradation of tetracycline in the photo-Fenton process

Xia Liu , Yuting Zhou, Shuanghui Sun and Siqi Bao*
Changchun Univ. Sci. & Technol., Sch Chem. & Environm. Engn., Changchun 130022, P. R. China. E-mail: baosiqi@cust.edu.cn

Received 12th August 2023 , Accepted 14th October 2023

First published on 30th October 2023


Abstract

An environment-friendly 3D NiFe-LDHs photocatalyst was fabricated via a simple hydrothermal method and characterized by means of SEM, XRD, BET, XPS and FT-IR. It is a highly efficient heterogeneous photo-Fenton catalyst for the degradation of TC-HCl under visible light irradiation. After exploring the effects of catalyst dosage, initial concentration of TC-HCl, solution pH and H2O2 concentrations, the optimal reaction conditions were determined. The experiment results showed that the degradation efficiency can reach 99.11% through adding H2O2 to constitute a photo-Fenton system after adsorption for 30 min and visible light for 60 min. After four cycles, the degradation rate decay is controlled within 21.2%, indicating that NiFe-LDHs have excellent reusable performance. The experimental results of environmental factors indicate that Fe2+ and Ca2+ promoted the degradation of TC-HCl, both Cl and CO32− inhibited the degradation of TC-HCl. Two other antibiotics (OTC and FT) were selected for research and found to be effectively removed in this system, achieving effective degradation of a variety of typical new pollutants. The radical trapping tests and ESR detection showed that ·OH and ·O2 were the main active substances for TC degradation in the photo-Fenton system. By further measuring the intermediate products of photodegradation, the degradation pathway of TC-HCl was inferred. The toxicity analysis demonstrated that the overall toxicity of the identified intermediates was reduced in this system. This study provides a theoretical and practical basis for the removal of TC in aquatic environments.


1. Introduction

Antibiotics are a type of drug that can effectively resist bacterial infections and are widely used in industries such as pharmaceuticals and livestock and poultry farming. Some of them, nevertheless, have not yet entirely assimilated and have infiltrated the aquatic environment. They have developed into one of nature's most deadly new water pollutants as a result.1–3 Due to its strong hydrophilicity and low volatility, tetracycline hydrochloride (TC-HCl), which is ranked second in the world in terms of manufacturing, exhibits excellent persistence in aqueous environments.4–6 If organisms cannot completely absorb antibiotics taken orally, the majority of them will be expelled from the body as metabolites or in their original form. Antibiotics will eventually infiltrate groundwater through leaching and infiltration after being used as organic fertilizer on agricultural land. Antibiotics, which are biodegradable compounds with high biological activity, persistence, and bioenrichment, have been identified as a novel contaminant in water environmental media. Antibiotic residues in water are present in trace amounts, but they will eventually build up and move up the food chain, harming the ecosystem and endangering human health. These effects include bacterial resistance growth, disruption of animal and plant growth and reproduction, chronic poisoning of the human body, and the “three causes” effect. China has emerged as the world's most substantial manufacturer and importer of antibiotics.7–9 As a result, one of the key issues that has to be resolved immediately in the field of environmental protection is the investigation of low-cost and effective advanced antibiotic residue treatment.

Currently, TC-HCl is predominantly destroyed by physical, chemical, and biological mechanisms.10 However, physical and biological techniques of material degradation are inadequate and contribute to additional contamination. Photocatalytic degradation methodology based on semiconductors has been demonstrated to be one of the chemical techniques used to breakdown pollutants due to its low cost and environmentally beneficial character.11–15 The hydroxyl radical (·OH) produced by the Fenton oxidation process has the benefit that it is not selective and can destroy the majority of organic contaminants in the environment. It positive aspects from robust interference blocking capabilities, a wide application window, mild reaction conditions, and simple operation. H2O and CO2 are the ultimate products of the Fenton oxidation process, which satisfies the environmental protection standards of “zero discharge” of wastewater.7,8 The heterogeneous Fenton, or Fenton-like technology, in particular, not only keeps the benefits of high activity and good stability. It also addresses the classic homogenous Fenton's technological problem bottleneck. The reaction between a photogenerated carrier, water, and oxygen molecules in the system provides the basis for heterogeneous Fenton's process, which results in the production of free radical active species with potent oxidizing properties.16 As a result, the absorbance of a material has a significant impact on the effectiveness of photocatalytic degradation. Tetracycline degradation of semiconductors with broad band gaps, such as ZnO, TiO2, and SnO2, has been extensively researched up to this point.17–19 However, the poor light consumption rate severely impedes their progress toward practical application, so it is crucial to figure out how to create unique, narrow band gap semiconductors that can effectively utilize the visible light region for TC-HCl degradation.

Layered double hydroxides (LDHs), described by the general formula [M1−x2+Mx3+(OH)2]x+ [Ax/nn·yH2O]x, where M2+, M3+ signify divalent and trivalent metal ions, respectively. The value of x is equal to the molar ratio of M3+/(M2+ + M3+), and An is an n-valent interlayer anion, have widely applied in area such as hydrogen evolution, fire retardants, water cracking and effluent remediation due to their unique layered structure and chemical properties.20–22 LDHs are a potential class of 3D materials because they have a large specific surface area with enough active sites for adsorbing pollutants as well as the ability to readily control the types of interlaminar ions and surface functional groups. Furthermore, by altering the interlayer ions of LDHs, it is possible to achieve the absorbability of the visible light region. For example, Feng et al. have prepared mesoporous NiFe-LDHs photocatalyst via a facile hydrothermal route and the results showed that NiFe-LDHs the as-prepared LDHs materials performed superior photocatalytic efficiency to eliminate TC from aqueous water solution.23 Yu et al. have synthesized MoS2/NiFe–Ni foam by simple electrodeposition and hydrothermal methods, which have a high degradation efficiency of dissolved TC by up to 92% during 100 min reaction time under visible light irradiation.24 A superior contender for a photocatalyst among the numerous LDHs is 3D NiFe-LDHs, which not only have high visible light absorption capabilities but also have better selective adsorption of pollutants than other LDHs.25,26 There are, however, few publications on the photocatalytic degradation of tetracycline by NiFe-LDHs, and it is necessary to further investigate and optimize the impact of environmental factors on degradation performance.

The development of 3D NiFe-LDHs nanoflowers was accomplished in the present investigation using a straightforward solvothermal method. The microscopic features such as morphology, crystal composition, types of surface functional groups and absorbance were investigated by SEM, XRD, XPS, FT-IR and UV-vis. Degradation measurements revealed that 3D NiFe-LDHs as synthesized have outstanding TC-HCl elimination efficiency in the photo-Fenton method. In-depth research was also done on the effects of photocatalyst concentration, reaction time, pH level, H2O2, common anions, and humic acids on photocatalytic degradation. It was investigated to determine how various antibiotic varieties and differences in water quality impacted the performance of the NiFe-LDHs in real-world applications. Finally, a free radical capture experiment, an electron spin resonance test, and the identification of intermediate products were performed to better understand the mechanism and pathway of TC degradation. This work promoted the transition from theory to practice by laying the theoretical groundwork for the improvement of 3D NiFe-LDHs photocatalytic degradation efficiency.

2. Materials and methods

2.1 Materials

Ni(NO3)2·6H2O, Fe(NO3)3·9H2O, NH4F, urea, and anhydrous methanol (≥99.5%) were of analytical grade and purchased from Shanghai Macklin Biochemical Co., Ltd. The tetracycline hydrochloride (TC-HCl), oxytetracycline (OTC) and nitrofurantoin (FT) were analytical reagents and purchased from Sinopharm Chemical Reagent Co., Ltd (the molecular information of TC, OTC and FT is shown in Table S1). All reagents were used as received without further purification.

2.2 Preparation and characterization of NiFe-LDHs

According to previously published literature.27 NiFe-LDHs was created using a hydrothermal process. In a typical synthesis, a clear salt solution with a Ni2+/Fe3+ molar ratio of 2.0 was created by dissolving Ni(NO3)2·6H2O (5.816 g) and Fe(NO3)3·9H2O (4.04 g) in methanol anhydrous (30 mL). The salt solution was immediately mixed with urea (1.261 g) and NH4F (0.1 g) and rapidly agitated for 2 hours. The solution was then placed to a 50 mL stainless steel autoclave that was lined with Teflon. For 12 hours, the autoclave was sealed and kept at 120 °C. By using a centrifugal technique, solid sediment was collected and subjected to three separate washes with distilled water and ethanol. Finally, drying in a vacuum oven produces brown powder particles. Characterization of NiFe-LDHs was provided in the ESI.

2.3 Catalytic degradation experiment

A 500 W xenon lamp from Anhongda Optoelectronics Technology Co., Ltd in China was used in a photoreaction apparatus that the researchers built themselves to conduct the photocatalytic degradation studies. The sample was 10 cm away from the xenon lamp, and 5000 Lex of light was being emitted. The following experiments were carried out: TC solution (50 mL) was mixed with magnetic stirrers to distribute 30 mg of NiFe-LDHs, and the required amount of H2O2 was then added. The mixture was agitated in the dark for 30 minutes prior to illumination to achieve adsorption equilibrium. The xenon lamp used to simulate sunshine was then held over the suspension. At predetermined intervals, a specific volume of analytical sample was quickly removed from the reaction solution and filtered through a 0.22 μm membrane. The maximum absorption band (356 nm) on a UV-vis spectrophotometer (Shanghai Yuefeng Instrument Co., Ltd, China) was used to determine the concentration of TC, and Lambert–Beer's law was used to determine the residue concentration of the TC solution. The following equation was used to compute the photocatalytic degradation efficiency (μ):
 
μ = (C0Ct)/C0 × 100% (1)
where C0 is the initial concentration of TC, and Ct is the TC concentration at the corresponding reaction time.

Other water quality investigations and other antibiotic experiments were conducted to evaluate the NiFe-LDHs' practical applicability. The initial photocatalytic reaction's settings were followed for the recycle testing. The synthesis and function of active species in the photo-Fenton process were investigated using quenching experiments and ESR tests, and the intermediate products of photodegradation were identified using UPLC/MS. The decomposition experiment of H2O2 was also carried out. After the experiment was completed, the solution was filtered out with filter paper, and the remaining catalyst was dried at 80 °C in the oven and kept at low temperature for recycling.

3. Results and discussion

3.1 Characterization of NiFe-LDHs

SEM measurements were employed to explore the morphology and crystal phase of NiFe-LDHs. As can be seen from Fig. 1a, the synthesized catalyst exhibits an abundant 3D sheet-like network structure, which is a flower-like microporous structure formed by the stacking of smooth thin nanosheets. In addition, the nanosheets are homogeneous in size and measure a thickness of about 30 nm. As described in literature, the observed highly connected sheet-like network may provide broad transportation paths for electron transfer.28 Furthermore, this three-dimensional structure, which resembles a flower, increases the number of reaction sites and makes adsorption reactions easier. Additionally, the catalyst's surface and interior offer various opportunities for the incident light to reflect and scatter, which enhances the use of visible light. The EDS element mapping maps corresponding to Ni, Fe, C and O in NiFe-LDHs are shown in Fig. 1 respectively. The contents of Ni, Fe, C and O are evenly distributed in the catalyst.
image file: d3ra05475f-f1.tif
Fig. 1 Structural characterizations of NiFe-LDHs. (a) SEM image, (b) XRD pattern, (c) FT-IR and (d) BET and aperture distribution.

In order to obtain the crystal structure of NiFe-LDHs, X-ray diffraction spectroscopy tests was conducted (Fig. 1b). There were obvious characteristic diffraction peaks at 2θ = 11.5°, 23.3°, 34.6°, 39.0°, 46.4°, 60.3°, 61.3° and 65.2°. It is consistent with (003), (006), (012), (015), (018), (110), (113) and (116) on the standard card of hexagonal system NiFe-LDHs (JCPDS 40-0215).29 And there were no other obvious peaks in the spectrogram, indicating that the purity of the prepared NiFe-LDHs is high.

FT-IR test further analyzed the surface chemical properties, the existence of functional groups, element composition and surface chemical bond of NiFe LDHs. As shown in Fig. 1c, a wide absorption peak was displayed at 3357 cm−1, which could be attributed to the O–H stretching mode of water molecules, with corresponding H–OH vibrations occurring at approximately 1622 cm−1. The strong peak at 1375 cm−1 corresponds to NO3, which conforms to the typical characteristics of LDHs.35–37

Fig. 1d shows BET and aperture distribution images of NiFe-LDHs. The curve is very similar to that of type IV. According to IUPAC classification, it belongs to H3 hysteresis loops, which is typical mesoporous material.38 The results of N2 adsorption show that NiFe-LDHs had a very high specific surface area (216.27 m2 g−1), and the pore size is mainly concentrated around 1.81 nm. The larger the specific surface area of the catalyst, the larger the contact area with organic pollutants, and then the more active sites involved in adsorption and photocatalytic reactions. Thus it can be seen that NiFe-LDHs is expected to achieve efficient degradation of pollutants.

XPS analysis was conducted to further investigate the composition and surface state of NiFe-LDHs. The wide scan survey spectra (Fig. 2a) verified the co-existence of Ni, Fe, C and O element. As shown in Fig. 2b, O element can be divided into two peaks by Gaussian fitting located at 531.9 eV and 533.5 eV, which corresponded to the lattice oxygen and surface chemisorbed oxygen, respectively.30 In C 1s spectra (Fig. 2c), the peaks at 284.5 eV, 286.1 eV and 288.4 eV could be assigned to C–C/C[double bond, length as m-dash]C, C–O and C[double bond, length as m-dash]O, respectively. The spectrum of Fe 2p (Fig. 2d), exhibited three fitted peaks at 711.49, 714.3, 725.98 eV and 733.9 eV, which corresponded to Fe(II), Fe(III), Fe(II) and Fe(III), respectively.31–33 Fig. 2e displayed that the fitting peaks of Ni 2p3/2 and Ni 2p1/2 were located at 855.4 eV and 873.3 eV, respectively, including two satellite peaks at 879.8 eV and 862.1 eV.32–34 What is more, because the presence of carbon, two satellite peaks around the main reflection appear at 880.4 eV and 862.1 eV.


image file: d3ra05475f-f2.tif
Fig. 2 (a) XPS survey spectra of 3D NiFe-LDHs; (b) XPS O 1s spectrum; (c) XPS C 1s spectrum; (d) XPS Fe 2p spectrum; (e) XPS Ni 2p spectrum.

The electrochemical test of NiFe-LDHs is depicted in Fig. S1. The UV-vis DRS test is a significant tool for characterizing light absorption performance since it allows you to see the range and intensity of the catalyst's light response. The estimated band gap of NiFe-LDHs is 2.08 eV, as shown in Fig. S1(a), and a narrower band gap is favourable to boosting the migration efficiency of photogenerated electrons, hence promoting the degradation of tetracycline hydrochloride. Fig. S1(b) shows that photoluminescence spectra were acquired at the excitation wavelength of 500 nm using a PL emission spectrum test to investigate the separation and transfer efficiency of the material's photogenerated electron hole pairs. The sample's linear scanning voltammetric curve (LSV) is shown in Fig. S1(c). The figure shows that NiFe-LDHs has the largest current density at the same point position, indicating the quickest electron transfer rate. Fig. S1(d) depicts the material's electrochemical impedance spectrum, which reveals that the synthesized NiFe-LDHs have a lower arc radius in the high frequency area than pure Ni(NO3)2 and Fe(NO3)3. According to the results of the foregoing electrochemical experiments, the synthesized NiFe-LDHs has a better electron transfer and separation efficiency, which is advantageous for the photocatalytic process.

3.2 TC degradation in the photo-Fenton process

3.2.1 Determination of optimum conditions. To investigate the effect of various NiFe-LDHs doses on the photo-Fenton degradation of TC-HCl, five different dosages of NiFe-LDHs were chosen. The degradation rate of TC increased from 3.95% to 63.69% when the dosage of NiFe-LDHs increased from 0 to 30 mg (Fig. 3a). However, the degradation rate of TC dropped from 63.69% to 53.74% as the catalyst dosage continued to increase to 50 mg. This is due to the fact that as the dosage of catalyst increased, the quantity of free radicals and holes generated also grew. Additionally, the contact sites between the catalyst and TC increased, which would promote degradation. However, as the amount of catalyst further increased, excessive catalyst could lead to aggregation, reduced the light transmission through the solution, hindered the production of active substances, and thus inhibited the degradation of TC.39
image file: d3ra05475f-f3.tif
Fig. 3 (a) Effect of NiFe-LDHs dosage on TC degradation in the photo-Fenton process. [TC] = 30 mg L−1, pH = 6.01 and H2O2 = 1 mmol L−1, (b) effect of effect of TC concentrations on TC degradation in the photo-Fenton process. NiFe-LDHs dosage = 30 mg, pH = 6.01 and H2O2 = 1 mmol L−1, (c) effect of pH on TC degradation in the photo-Fenton process. NiFe-LDHs dosage = 30 mg, [TC] = 30 mg L−1 and H2O2 = 1 mmol L−1, (d) effect of H2O2 concentrations on TC degradation in the photo-Fenton process. NiFe-LDHs dosage = 30 mg, [TC] = 30 mg L−1 and pH = 8.01.

The results of the effects of various initial TC concentrations are displayed in Fig. 3b. The degradation rate increased from 69.47% to 88.69% when the starting concentration of TC increased from 10 mg L−1 to 30 mg L−1. The degradation rate decreased from 88.69% to 55.27% as the starting concentration of TC HCl increased to 70 mg L−1. The reason for this phenomenon is that within the low concentration range, as TC concentration increased, the stimulated TC molecules and reactive oxygen species generated by irradiation increased, which boosted photodegradation. However, as TC concentration continued to increase, the color deepening of the solution would impact the transmittance, which was not conducive to the photocatalytic reaction and inhibited the degradation of tetracycline.

The impact of various initial pH levels on the photo-Fenton degradation of TC is depicted in Fig. 3c. In more detail, weak alkalinity facilitated the process, while both acidic and alkaline circumstances prevented it. This is because when the solution weakly alkaline (pH = 8.01), the catalyst was relatively stable, which was conducive to promoting the catalytic performance of the photocatalyst. The lower left corner of Fig. 3c depicts the morphological distribution curve of TC in aqueous solutions as a function of pH. TC is also an amphoteric chemical that exists in many forms under various pH settings.40 The isoelectric point of NiFe-LDHs was calculated to be 6.97 by calculating the pH-zeta curve (Fig. S2). When the pH was at 2.09 and 4.2 (smaller than the isoelectric point), the surface of NiFe-LDHs was positively charged due to zwitterions protonation, and the TC was in a cationic condition. As a result, a electrostatic repulsion was showed, which hindered deterioration. The surface of NiFe-LDHs was negatively charged when the pH was 10.04 (higher than the isoelectric point). TC was in an anionic form (TCH) at this stage, and NiFe-LDHs and TC were mutually exclusive. Furthermore, under alkaline conditions, the degree of deprotonation of tetracycline increases, resulting in a decrease in its breakdown rate.41,42

The influence of varying H2O2 concentrations on photo-Fenton degradation of TC is shown in Fig. 3d. By raising the H2O2 concentration from 1 mmol L−1 to 3 mmol L−1, the degradation rate rose from 68.01% to 99.11%. However, when the H2O2 concentration was increased to 4 mmol L−1, the degradation rate did not alter considerably. This is due to the fact that under transition metal conditions, H2O2 can form hydroxyl radicals (·OH), which promote the decomposition of pollutants. As the concentration of H2O2 increased, ·OH generation increased. However, as the concentration of H2O2 continued to increase, excess H2O2 in the system depleted ·OH in the system, causing the reaction rate no longer increased. The findings are consistent with prior findings.43 Therefore, from the perspective of environmental protection, 3 mmol L−1 is selected as the optimal concentration of H2O2 to continue the follow-up experiment.

3.2.2 Degradation performance of TC under the optimum conditions. Batch studies were carried out to investigate the degradation of TC in various settings, and the findings are given in Fig. 4a. It is obvious from Fig. 4a that TC did not degrade fundamentally under visible light, showing that TC was resistant to visible light. The degradation of TC was marginally accelerated with the addition of H2O2 to the solution, which probably because H2O2 created ·OH under light circumstances, encouraging the breakdown of TC. When Ni2+ + Fe3+ and H2O2 are added to the system under light conditions, approximately 71% of the tetracycline is eliminated; however, Ni2+ and Fe3+ added to the homogeneous system will all dissolve in the reaction solution and are difficult to recover after the reaction, requiring additional experimental expenses. In the NiFe LDHs/vis system, the degradation rate of TC reached 68.01% due to the photocatalytic effect. With the addition of H2O2 to the solution, the rate of TC degradation was further accelerated and eventually reached 99.11%, which is a typical heterogeneous photo-Fenton process. The apparent rate constant of TC degradation was estimated by fitting pseudo first order, and the results are shown in Fig. 4b. The outcomes demonstrated that all reactions adhered to the first-order kinetic equations. The first-order kinetic constant of TC in the photo-Fenton system is 4.09 times than that of the NiFe-LDHs/vis system, indicating that H2O2 played a significant role in the formation of active species. Additionally, the k of the NiFe-LDHs/H2O2/vis system is 13.2 times than that of the NiFe-LDHs/H2O2 system, demonstrating that visible light can encourage the formation of charge carriers, thereby promoting degradation. The characteristics of NiFe-LDHs are compared to those of other photocatalytic materials in Table 1. It is apparent from the analyses done that this effort has produced a suitable photocatalyst.
image file: d3ra05475f-f4.tif
Fig. 4 (a) Degradation of TC in different systems, (b) reaction kinetics fitting curves.
Table 1 Comparison of the present research with similar studies done before
Material Light source Working solution Degradation rate pH Ref.
P–CdS@NiFe-LDH 300 W Xe lamp 30 mg photocatalyst 30 mL MO (10 mg L−1) 98% (100 min) 44
FeCoZnO4/CuCr-LDH Vis-light(λ ≥ 400 nm) 0.5 g L−1 catalyst 50 μM caffeine 66.5% (120 min) 8 45
Fe2O3/Zn–Al-LDH UV-vis-light 0.01 g catalyst 100 mL OII (40 mg L−1) 81.2% (5 h) 6.7 46
Cu–Zn–Fe-LDH UV-vis-light 0.5 g L−1 catalyst 250 mL PR and arsenic (1 mg L−1) 99% (10 h) 7 47
FePcS-PMA-LDH 500 W Xe lamp 40 mg catalyst 100 mL BPA (10 mg L−1) 100% (100 min) 6 48
ND/CuFe-LDH 500 W Xe lamp 0.0667 g L−1 75 mL MB (10 mg L−1) 93.5% (120 min) 49
M3Cr–CO3-LDH 150 W halogen lamp 0.5 g catalyst 25 mg MB (5 mg L−1) 90.67 (140 min) 50
(Co–Mg)Al-LDH UV-vis-light 0.05 g catalyst 500 mL solvent 10% (5 h) 51
MnMgFe-LDH UV-vis-light 30 mg catalyst 100 mL MB (20 ppm) 92% (300 min) 7 52
NiFe-LDH 500 W Xe lamp 30 mg catalyst 50 mL TC (30 mg L−1) 99.11 (90 min) 6.01 This work


3.2.3 Effect of environmental factors on TC degradation. Since multiple ions and humic acid are ubiquitous in the water environment, the influence of four typical inorganic ions (Cl, CO32−, Fe2+ and Ca2+) and humic acid (HA) on TC degradation in LDHs/H2O2/vis system was studied.53 It is obviously observed that the degradation of TC was inhibited after the addition of Cl and CO32−. The reason is that Cl and CO32− consume ·OH in the system as scavengers of ·OH (eqn (2)–(5)).53,54 On the contrary, the presence of Fe2+ and Ca2+ promoted the degradation of TC. The facilitation of Fe2+ because it reacts with dissolved oxygen in the system to generate superoxide anion radicals (·O2) and Fe3+ (eqn (6) and (7)), and Fe3+ can further generate ·OH under visible light, promoting degradation. Ca2+ exhibited an enhancing effect because Ca2+ could recombine with N4–OH12a on the A ring and the O10–O12 on the BCD ring of TC (upper right corner of Fig. 5), thereby depleting tetracycline hydrochloride TC and promoting degradation.55,56 Low concentration (5 mg L−1) of HA played a promoting role, and high concentration (20 mg L−1) played an inhibitory role. This is because HA has both photosensitizing and shading effects. Photosensitization is due to that HA generated ·OH, H2O2 and ·O2 through type I (eqn (8)) and 1O2 through type II (eqn(9)), and these active substances generated promoted the degradation of TC.60 Instead, HA competed with TC for active groups to inhibit degradation. Therefore, the role of HA in the photo-Fenton degradation of TC depends on the balance between the two opposite effects.57
 
·OH + Cl → Cl· + OH (2)
 
CO32− + H+ → HCO3 (3)
 
HCO3 + ·OH → H2O + CO3 (4)
 
CO32− + ·OH → OH + CO3 (5)
 
Fe2+ + hv → Fe3+ + e (6)
 
O2 + Fe2+ → Fe3+ + ·O2 (7)
 
image file: d3ra05475f-t1.tif(8)
 
image file: d3ra05475f-t2.tif(9)

image file: d3ra05475f-f5.tif
Fig. 5 Effect of anions, cations and HA on TC degradation in the photo-Fenton process.
3.2.4 Environmental compatibility. Four different water quality were chosen: tap water, pure water (Wahaha water), automobile factory wastewater (the water quality is provided in Table S2), and domestic sewage, and the degradation rates were 83.66%, 83.66%, 74.04%, and 74.04%, respectively (Fig. S3(a)). Under different water quality conditions, the removal of TC showed relatively ideal results. However, due to the complexity of its components, domestic sewage and automobile factory wastewater exhibited a significant inhibitory effect on the decomposition of TC compared to distilled water. Hence one can see that NiFe LDHs can effectively decompose TC contaminants in various water qualities. Furthermore, two other antibiotic pollutants, OTC and FT were selected to study. It can be seen from Fig. S3(b) that NiFe-LDHs has a good degradation effect not only on TC, but also on OTC and FT, which verifies the broad spectrum of NiFe-LDHs and has the potential to degrade more antibiotic pollutants.

To investigate the stability of NiFe-LDHs, six cycle experiments were performed. NiFe-LDHs showed good stability after repeated degradation of TC for six times (Fig. 6). At the end of the sixth cycle experiment, the degradation rate of TC was 75.99%, which was lower than that of the first photocatalytic experiment (99.11%). This may be related to the dissolution of metal ions, the adsorption of reaction intermediates and the loss of catalysts during centrifugation.58 Moreover, during the cycle experiment, the adsorption performance of the catalyst continue to decrease, which also affect the degradation rate of TC. However, the performance of the catalyst did not degrade much after the six cycles of the experiment, and the degradation performance remained stable after that. Fig. S4 shows the XPS spectra of NiFe-LDHs after 6 cycles. We can see that Ni, Fe, C and O elements in the XPS spectra before and after the reaction do not change, but the peak height and peak area change slightly, indicating that REDOX reactions occur on the surface of the material. At the same time, the content changes of nickel and iron ions before and after the reaction were calculated, as shown in Table S4. It can be found from the table that for nickel ion, the percentage of Ni2+ and Ni3+ before the reaction is 24.0% and 75.1% respectively, while the percentage of Ni2+ and Ni3+ after the reaction is 37.85% and 62.15% respectively, indicating that 12.95% of Ni3+ is converted into Ni2+. Similarly, for iron ion, 18.11% of Fe2+ was converted to Fe3+. The ionic leaching amounts of Ni2+ and Fe3+ were further determined. After 6 cycles of experiments, the ion leaching amounts of Ni2+ and Fe3+ decreased to 3.92 mg L−1 and 3.14 mg L−1, respectively, and the ion leaching amounts were still reduced. However, both leaching amounts are slightly higher than international standards. There are two primary causes of metal ion leaching: (1) during the reaction process, the valence state of metal REDOX decreases, resulting in a change in the chemical characteristics of the corresponding metal elements, resulting in metal ion leaching;59 (2) because the sample is shipped to other institutes for analysis, the extended soaking time causes solution evaporation and corrosion of the metal material, resulting in an increase in the metal leaching amount that is greater than the real metal leaching amount. In future trials, we plan to mix NiFe-LDHs with additional materials to further limit metal leaching.60 In future trials, we intend to further reduce the amount of ion leaching by mixing it with other materials, with the goal of meeting national standards. To properly comprehend the stability feature, SEM and XRD characterizations of fresh and after 6 runs NiFe-LDHs were examined. As can be seen in Fig. S5(a), although the characteristic diffraction peak overall diminished, the XRD patterns showed that the crystal structure of NiFe-LDHs was still intact. This may be because the crystal form deteriorated during continuous run. In addition, after six cycles, the morphology of three-dimensional nano-flowers changed, as shown in Fig. S5(b), which may be caused by structural collapse during the reaction process. Overall, NiFe-LDHs has good stability, recyclability and prospects in practical applications.


image file: d3ra05475f-f6.tif
Fig. 6 Recycling experiments of NiFe-LDHs in the photo-Fenton process.

3.3 The possible mechanism of TC degradation

The quenching experiments of active substance (ROS) were carried out to study the degradation mechanism. Ammonium oxalate (AOM), p-benzoquinone (p-BQ), furfuryl alcohol (FA), ethanol (EtOH) and tert-butanol (TBA) are added to the system as quenchers for h+, ·O2, 1O2, catalyst surface ·OH and solution ·OH, respectively.61 It can be seen from Fig. 7a that the addition of five quenchers all had different inhibitory effects on the degradation of TC, among which ethanol and p-BQ showed the greatest inhibitory effects, indicating that catalyst surface ·OH and ·O2 were the main active substances in the system. Subsequently, ESR tests were performed to observe the magnetic resonance signal of electrons by comparing the dark and visible light conditions, so as to verify the active free radicals that play major roles in the system. The ESR signals of DMPO-·OH and DMPO-·O2 did not show obvious ESR signals under dark conditions (Fig. 7b and c). On the contrary, both DMPO-·OH and DMPO-·O2 showed strong signal peaks under visible light, demonstrating that ·O2 and ·OH are the main active substances, which is consistent with the results of the quenching experiments.62 Furthermore, the breakdown of H2O2 was determined. The decomposition of H2O2 was further determined, as shown in Fig. S6. The experimental results show that the self-decomposition rate of H2O2 is 14.35%, indicating that H2O2 mainly promotes the formation of active substances through the REDOX reaction with NiFe-LDHs, resulting in the valence transformation of metals, thus promoting the catalytic reaction.
image file: d3ra05475f-f7.tif
Fig. 7 The effects of different scavengers on TC degradation in the photo-Fenton process and EPR spectra of (b) DMPO-·OH, (c) DMPO-·O2.

The degradation mechanisms are depicted in Fig. 8. At the initial stage of the reaction, 17.4% of TC was adsorbed onto catalyst surface due to its substantial specific surface area. NiFe-LDHs then produced photo-generated electrons (e) and photo-generated holes (h+) in the presence of visible light (eqn (10)).63 Subsequently, h+ reacted with H2O or OH in the system to produce ·OH (eqn (11) and (12)). e reacted with ·O2 on the catalyst surface to form ·O2 (eqn (13)), and then generated ·OH with stronger oxidation capacity (eqn (14)–(16)). Additionally, H2O2, a potent oxidant, can substantially lower the chances of e and h+ recombination and produce a significant amount of ·OH to support photocatalyst activity (eqn (17)).64 Under visible light, Fe3+ can simultaneously produce ·OH and Fe2+ (eqn (18)), which is necessary for the subsequent heterogeneous Fenton reaction (eqn (19)).65 Fe (III/II) and Ni (II/III) conversion during the entire reaction phase sped up the reaction (eqn (19)–(23)). In order for TC to entirely degrade into small molecules or even completely mineralize into CO2 and H2O (eqn (24)), the produced ·OH and ·O2 attacked the bonds in TC that are difficult to break.

 
3D NiFe-LDHs + hv → 3D NiFeLDHs (h+ + e) (10)
 
h+ + H2O → H+ + ·OH (11)
 
h+ + OH → ·OH (12)
 
O2 + e → ·O2 (13)
 
image file: d3ra05475f-t3.tif(14)
 
image file: d3ra05475f-t4.tif(15)
 
image file: d3ra05475f-t5.tif(16)
 
H2O2 + visible light → ·OH + OH (17)
 
Fe3+ + OH + hv → Fe2+ + ·OH (18)
 
Fe2+ + H2O2 → Fe3+ + ·OH + OH (19)
 
Fe3+ + H2O2 → Fe2+ + ·OOH + 2H+ (20)
 
Ni2+ + H2O2 → Ni3+ + ·OH + OH (21)
 
Ni3+ + H2O2 → Ni2+ + ·OOH + OH (22)
 
Ni3+ + Fe2+ → Ni2+ + Fe3+ (23)
 
·OH/·O2 + TC–HCl → byproducts + CO2 + H2O (24)


image file: d3ra05475f-f8.tif
Fig. 8 Proposed mechanisms of the degradation of TC in the photo-Fenton process.

3.4 The possible degradation pathway of TC and toxicity analysis

Based on the detection of intermediates by UPLC-MS (Table S3) and previous literature reports.66–68 three potential degradation pathways were speculated, as shown in Fig. 9. Three potential degradation pathways were suggested, and a total of seven stable intermediate products were found. For process 1, tetracycline undergoes h+-induced demethylation, oxidation and dehydration reaction, which results in continual ring-opening and eventual decarboxylation, to yield the intermediate (m/z = 246).69 The tetracycline molecule undergoes demethylation, deamination, and hydroxylation to yield the intermediate (m/z = 221) for process 2. The third method involves first releasing the C[double bond, length as m-dash]C bond from the tetracycline molecule, followed by the removal of the amide group to produce the related intermediate (m/z = 262). The different intermediates are ultimately totally reduced into the environmentally favorable substances CO2 and H2O by further oxidation into smaller molecules (m/z = 218, 165, 146, and 85).
image file: d3ra05475f-f9.tif
Fig. 9 Potential degradation pathways of TC in the photo-Fenton process.

The lethal concentrations of 50% fathead minnow (LC50-96 h) and daphnia magna (LC50-48 h) were evaluated by Toxicity Estimation Software Tool (TEST) based on QSAR to determine the toxicity of TC and intermediates (Fig. 10a and b).70 The calculations revealed that the lethal concentrations of the intermediates were much lower than those of TC, except for P2, P3, P4 (LC50-96 h) and P2, P4, P10 (LC50-48 h).71 Fig. 10c demonstrates that the developmental toxicity of intermediates was greatly decreased compared to TC, with the exception of P2, P3, P4, and P8, and P9, P10, and P12 (ref. 72) even becoming “developmental non-toxic.” TC, P1, P2, P4, and P11 were positive in terms of mutagenicity (Fig. 10d), whereas the mutagenicity of other intermediates changed from positive to negative. The toxicity prediction stated above states that while some intermediates are still dangerous, they can be totally converted into intermediates that are less toxic by prolonging the reaction period. As a result, the total toxicity of TC was reduced in the photo-Fenton process.


image file: d3ra05475f-f10.tif
Fig. 10 The fathead minnow LC 50–96 h (a), daphnia magna LC50-48 h (b), developmental toxicity (c) and mutagenicity (d) of tetracycline and its possible degradation intermediates.

4. Conclusion

By optimizing the reaction conditions, flower-like structured NiFe-LDHs was fabricated in this study using a one-step hydrothermal technique for effective TC elimination in the photo-Fenton process. Under optimal conditions, the NiFe-LDHs/H2O2/vis system performed well with very high efficiency, and the degradation rate of TC reached 99.11% within 90 minutes, which is superior to other reported materials. Meanwhile, this high activity of NiFe-LDHs was also suitable for multiple refractory antibiotic, different water quality conditions, and could maintain even in presence of various environmental anions and HA. The heterogeneous catalyst NiFe-LDHs was simple to recover following the reaction, and the amount of nickel and iron ions that leached were relatively low. It can be recycled and maintain excellent catalytic stability and reusability in the subsequent 6 reactions, showing enormous potential in real-world wastewater treatment. The separation of photogenerated carriers and the production of ROS, which aided in the degradation of TC, were encouraged by the Ni(II/III)/Fe(II/III) cycle on the surface of NiFe-LDHs. According to quenching experiments and EPR analysis, photogenerated h+, ·O2, ·OH, and 1O2 all took part in the process and ·OH and ·O2 dominated the breakdown of TC. Through LC-MS recognization of potential intermediates and TEST toxicity analysis, it was found that the degradation of TC by NiFe-LDHs in the photo-Fenton process is a reaction with significantly reduced toxicity. In subsequent experiments, NiFe-LDH needs to be modified to further accelerate the degradation rate of TC and reduce the leaching amount of metal ions.

Conflicts of interest

There are no conflicts to declare.

Acknowledgements

This work was financially supported by Joint Fund Project of the Natural Science Foundation of Jilin Province (YDZJ202101ZYTS076).

References

  1. N. Chandel, V. Ahuja and R. Gurav, Sci. Total Environ., 2022, 825, 153895 CrossRef CAS PubMed .
  2. W. Zhou, B. Yang and G. Liu, J. Colloid Interface Sci., 2022, 615, 849–864 CrossRef CAS PubMed .
  3. Z. Qi, G. Li and M. Wang, Water Res., 2022, 215, 118240 CrossRef CAS PubMed .
  4. D. Zheng, G. Yin and M. Liu, Sci. Total Environ., 2021, 777, 146009 CrossRef CAS PubMed .
  5. M. Habibi, A. Habibi-Yangjeh and S. R. Pouran, Colloids Surf., A, 2022, 642, 128640 CrossRef CAS .
  6. X. Liu, Q. Li and Y. Fan, Mater. Lett., 2022, 315, 132010 CrossRef CAS .
  7. S. Nasseri, A. H. Mahvi and M. Seyedsalehi, J. Mol. Liq., 2017, 241, 704–714 CrossRef CAS .
  8. Y. Wang, L. Wang and Z. Xiao, J. Alloys Compd., 2022, 900, 163450 CrossRef CAS .
  9. D. P. Sahoo, S. Patnaik and K. Parida, ACS Omega, 2019, 4(12), 14721–14741 CrossRef CAS PubMed .
  10. A. Zaher, M. Taha and R. K. Mahmoud, J. Mol. Liq., 2021, 322, 114546 CrossRef CAS .
  11. A. Tiwari, A. Shukla and D. Tiwari, J. Ind. Eng. Chem., 2019, 69, 141–152 CrossRef CAS .
  12. Y. Liu, J. Tian and L. Wei, Sep. Purif. Technol., 2021, 257, 117976 CrossRef CAS .
  13. N. Farhadian, R. Akbarzadeh and M. Pirsaheb, Int. J. Biol. Macromol., 2019, 132, 360–373 CrossRef CAS PubMed .
  14. Y. Li, Z. Lai and Z. Huang, Appl. Surf. Sci., 2021, 550, 149342 CrossRef CAS .
  15. S. Das and Y. H. Ahn, Chemosphere, 2022, 291, 132870 CrossRef CAS PubMed .
  16. S. Wu, X. Li and Y. Tian, Chem. Eng. J., 2021, 406, 126747 CrossRef CAS .
  17. A. Zyoud, W. Jondi and N. AlDaqqah, Solid State Sci., 2017, 74, 131–143 CrossRef CAS .
  18. Y. Li, Q. Zhang and Y. Lu, Ceram. Int., 2022, 48(1), 1306–1313 CrossRef CAS .
  19. A. O. Oluwole and O. S. Olatunji, Environ. Sci. Eur., 2022, 34, 1–14 CrossRef .
  20. Y. Yu, D. Chen and W. Xu, J. Hazard. Mater., 2021, 416, 126183 CrossRef CAS PubMed .
  21. C. Liu, S. Mao and M. Shi, J. Hazard. Mater., 2021, 420, 126613 CrossRef CAS PubMed .
  22. J. O. Eniola, R. Kumar and O. A. Mohamed, J. Saudi Chem. Soc., 2020, 24(1), 139–150 CrossRef CAS .
  23. X. Feng, X. Li and H. Luo, J. Solid State Chem., 2022, 307, 122827 CrossRef CAS .
  24. J. Yu, S. Cong and B. Liu, J. Environ. Chem. Eng., 2022, 10, 108437 CrossRef CAS .
  25. H. Wang, Y. Chen and W. Xie, Int. J. Electrochem. Sci., 2019, 14, 7961–7972 CrossRef CAS .
  26. F. Pazoki, S. Bagheri and M. Shamsayei, Mater. Chem. Phys., 2020, 253, 123327 CrossRef CAS .
  27. S. Anantharaj, K. Karthick and M. Venkatesh, Nano Energy, 2017, 39, 30–43 CrossRef CAS .
  28. S. He, R. Yin and Y. Chen, Chem. Eng. J., 2021, 423, 130172 CrossRef CAS .
  29. Q. Wang and D. O'Hare, Chem. Rev., 2012, 112(7), 4124–4155 CrossRef CAS PubMed .
  30. C. Lei, W. Li and G. Wang, Chem. Res. Chin. Univ., 2021, 37, 293–297 CrossRef CAS .
  31. N. Yang, C. Tang and K. Wang, Nano Res., 2016, 9, 3346–3354 CrossRef CAS .
  32. C. Xiao, Y. Li and X. Lu, Adv. Funct. Mater., 2016, 26(20), 3515–3523 CrossRef CAS .
  33. L. Zhang, R. Zhang and R. Ge, Chem. – Eur. J., 2017, 23(48), 11499–11503 CrossRef CAS PubMed .
  34. A. N. Mansour, Surf. Sci. Spectra, 1994, 3(3), 231–238 CrossRef CAS .
  35. A. Khataee, T. S. Rad and S. Nikzat, Chem. Eng. J., 2019, 375, 122102 CrossRef CAS .
  36. D. Huang, J. Ma and L. Yu, Sep. Purif. Technol., 2015, 156, 789–794 CrossRef CAS .
  37. K. M. Parida, M. Sahoo and S. Singha, J. Mol. Catal. A: Chem., 2010, 329(1–2), 7–12 CrossRef CAS .
  38. L. Liu, S. Li and Y. An, Catalysts, 2019, 9(2), 118 CrossRef .
  39. R. J. Watts and S. E. Dilly, J. Hazard. Mater., 1996, 51(1–3), 209–224 CrossRef CAS .
  40. Z. Li, C. Guo and J. Lyu, J. Hazard. Mater., 2019, 373, 85–96 CrossRef CAS PubMed .
  41. T. Soltani, A. Tayyebi and B. K. Lee, Environ. Manage., 2019, 232, 713–721 CAS .
  42. L. Chen, D. Ding and C. Liu, Chem. Eng. J., 2018, 334, 273–284 CrossRef CAS .
  43. I. Velo-Gala, J. A. Pirán-Montaño and J. Rivera-Utrilla, Chem. Eng. J., 2017, 323, 605–617 CrossRef CAS .
  44. C. Lai, F. Huang and G. Zeng, Chemosphere, 2019, 224, 910–921 CrossRef CAS PubMed .
  45. B. Fang, Z. Xing, M. Guo and Y. Qiu, Sep. Purif. Technol., 2021, 274, 119066 CrossRef CAS .
  46. A. Fazli, M. Brigante, A. Khataee and G. Mailhot, Chemosphere, 2022, 291, 132920 CrossRef CAS PubMed .
  47. Q. Li, G. Wei, Y. Yang, Z. Li, L. Zhang, L. Shao and S. Lai, Catal. Sci. Technol., 2020, 10(21), 313–534 CrossRef .
  48. H. Lu, Z. Zhu, H. Zhang and J. Zhu, ACS Appl. Mater. Interfaces, 2016, 8(38), 25343–25352 CrossRef CAS PubMed .
  49. F. Huang, S. Tian, Y. Qi, E. Li, L. Zhou and Y. Qiu, Materials, 2020, 13(8), 1951 CrossRef CAS PubMed .
  50. L. Liu, S. Li and Y. An, Catalysts, 2019, 9(2), 118 CrossRef .
  51. G. Pan, M. Xu, K. Zhou and Y. Meng, Clays Clay Miner., 2019, 67, 340–347 CrossRef CAS .
  52. R. Ionescu, O. D. Pavel, R. Bîrjega and R. Zăvoianu, Catal. Lett., 2009, 134, 309–317 CrossRef .
  53. R. G. L. Gonçalves, H. M. Mendes and S. L. Bastos, Appl. Clay Sci., 2020, 187, 105477 CrossRef .
  54. Y. H. Guan, J. Ma, D. K. Liu, Z. F. Ou, W. Zhang, X. L. Gong, Q. Fu and J. C. Crittenden, Chem. Eng. J., 2018, 352, 477–489 CrossRef CAS .
  55. M. E. Parolo, M. J. Avena and G. R. Pettinari, J. Colloid Interface Sci., 2012, 368(1), 420–426 CrossRef CAS PubMed .
  56. J. M. Wessels, W. E. Ford and W. Szymczak, J. Phys. Chem. B, 1998, 102(46), 9323–9331 CrossRef CAS .
  57. Y. Yang, X. Hu and Y. Zhao, J. Colloid Interface Sci., 2017, 495, 68–77 CrossRef CAS PubMed .
  58. R. Wang, F. Chen and L. Gao, J. Environ. Chem. Eng., 2022, 10, 108361 CrossRef CAS .
  59. Q. R. Liu, X. G. Duan and H. Q. Sun, J. Phys. Chem. C, 2016, 120(30), 16871–16878 CrossRef CAS .
  60. X. G. Duan, C. Su and J. Miao, Appl. Catal., B, 2018, 220, 626–634 CrossRef CAS .
  61. H. Sun, L. Wang and F. Guo, J. Alloys Compd., 2020, 900, 163410 CrossRef .
  62. J. Pan, L. Wang and Y. Shi, Sep. Purif. Technol., 2022, 284, 120270 CrossRef CAS .
  63. F. Guo, Z. Chen and X. Huang, Sep. Purif. Technol., 2021, 275, 119223 CrossRef CAS .
  64. W. Shi, C. Hao and Y. Shi, Sep. Purif. Technol., 2023, 304, 122337 CrossRef CAS .
  65. W. Shi, W. Sun and Y. Liu, J. Hazard. Mater., 2022, 436, 129141 CrossRef CAS PubMed .
  66. M. Shakeel, M. Arif and G. Yasin, Appl. Catal., B, 2019, 242, 485–498 CrossRef CAS .
  67. J. Shi, X. Liu and X. Bai, Fuel, 2021, 306, 121688 CrossRef CAS .
  68. S. He, R. Yin and Y. Chen, Chem. Eng. J., 2021, 423, 130172 CrossRef CAS .
  69. G. Yang, Y. A. Zhu and Y. Liang, Appl. Surf. Sci., 2021, 539, 148038 CrossRef CAS .
  70. S. Xin, G. Liu and X. Ma, Appl. Catal., B, 2021, 280, 119386 CrossRef CAS .
  71. S. Xin, B. Ma and G. Liu, J. Environ. Manage., 2021, 285, 112093 CrossRef CAS PubMed .
  72. Y. Gao, J. Zhang and J. Zhou, RSC Adv., 2020, 10, 20991 RSC .

Footnotes

Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d3ra05475f
Co-first authors.

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