Novel cost-effective catalyst granular activated carbon (GAC)-based zinc ferro nanocomposites for the heterogeneous Fenton's oxidation of dye were synthesized using bioleached laterite iron (BLFe) as a precursor and Psidium gujava leaf extract. Synthesized nanocomposites were characterized using SEM, EDS, XRD and BET surface area analysis. The degradation of Rhodamine dye was carried out with nanocomposites using adsorption–Fenton's oxidation process. The catalytic role of nanocomposites in Fenton's oxidation of Rhodamine B (RhB) was investigated and reported. The maximum dye removal of 96.2% was observed with 64.2% COD removal within 200 min of treatment. An increase in nanocomposite dosage has a positive effect on dye removal marking 5 g/L as an optimum dosage. Adsorption studies reveal that RhB removal using BLFe-based GAC/zinc ferro composites fits the Freundlich Adsorption Isotherm model with an adsorption capacity of 47.81 mg/g. A combination of adsorption and Fenton's oxidation has resulted in higher removal efficiency with nanocomposite material. Reusability studies confirm that the spent catalyst can be reused for five cycles.

  • Synthesis of novel GAC–zinc ferro composites.

  • Characterization of synthesized nanocomposites.

  • Removal of Rhodamine B using adsorption–Fenton's oxidation process.

Graphical Abstract

Graphical Abstract
Graphical Abstract

Contamination of environmental chemicals of dye from the textile industries is reflected in the usage of synthetic dyes for textiles (Dutta & Mukhopadhyay 2001). The complex structure of synthetic azo dyes is making them recalcitrant for degradation. Rhodamine B (RhB), N-[9-(2-carboxyphenyl)-6-(diethylamino)-3H-xanthen-3-ylidene]-N-ethylethanaminium, a unique fluorescent organic chloride salt dye that belongs to the group of xanthene dyes with its vast application in the textile industries (Table 1; Su et al. 2013). The fluorescence of RhB is temperature-dependent making it fluxional at room temperature. Direct discharge of processed water contaminated with dyes into natural streams harms biodiversity alarming potential danger to aquatic life (Islam & Mostafa 2018). RhB with poor biodegradability has extensive application in the paints and textile industries (Al-gheethi et al. 2022). The presence of RhD in natural streams indicates the direct discharge of industrial effluent to the natural stream posing threat to the aquatic environment (Hikmat et al. 2017).

Table 1

Details of Rhodamine B

DyeRhodamine B
Appearance Red to violet 
Molecular weight 479.0 
Molecular formula C28H31CIN2O3 
Structural formula  
Solubility in water (mg/L) 50 
DyeRhodamine B
Appearance Red to violet 
Molecular weight 479.0 
Molecular formula C28H31CIN2O3 
Structural formula  
Solubility in water (mg/L) 50 

Treatment of wastewater contaminated with dye demands sophisticated treatment remedy techniques as traditional treatment fails to cope with the issues. Filtration, a biological treatment, is proven to be inefficient for dye removal. The advanced oxidation process uses a strong oxidizing agent to degrade a large number of organic pollutants persistent for other methods of treatment. However, several modifications have been made and experimentation was carried out has been by various research teams to make the process more efficient and cost-effective. Nano iron particles were proven to be efficient in the Fenton's oxidation with effective reduction in treatment time (Sangami & Manu 2017, 2018).

The use of modified nano catalysts like nanocomposites, carbon-based iron–graphene oxides and carbon gel doped with iron were found to be very effective in organic pollutant degradation (Ahmadi et al. 2021; Karim et al. 2022). Hassani et al. synthesized cobalt ferrite–graphene oxide nanocomposites using a surfactant-based thermal decomposition–reduction technique and achieved 90.5% of efficiency in organic dye removal. The team also limits the reusability of nanocomposites for five consecutive cycles with drop in 22% of removal efficiency (Hassani et al. 2017). Removal of the dye RhB by Fenton's oxidation has been reported by previous researchers (AlHamedi et al. 2009; Xue et al. 2009; Bhaskar et al. 2022). AlHamedi et al. (2009) studied the decoloration of RhB with UV/H2O2 process in the absence of catalyst and reported 73% of efficiency. Bhaskar et al. (2022) investigated EDTA-based biojarosite-driven Fenton's and UV–Fenton's oxidation of RhB claiming 80.0% of removal efficiency in near neutral pH. This marks the role of iron catalyst in Fenton's oxidation for RhB removal. Adsorption is known for dye removal in textile wastewater (Uddin et al. 2021; Velusamy et al. 2021). The combination of Fenton's oxidation and adsorption enhances the treatment efficiency (Nair & Kurian 2017; Rahimpour et al. 2020). Nair & Kurian (2017) investigated catalytic oxidation with nickel zinc ferrite nanocomposites claiming zinc doping increased the oxidizing power and surface acidity of nickel increased catalytic efficiency. Catalytic replacement of commercial iron from laterite iron in the Fenton's degradation has been studied and reported (Karale et al. 2014; Sangami & Manu 2018; Bhaskar et al. 2021). The usage potential of biogenic jarosite on EDTA-based Fenton's oxidation for the removal of RhB dye was studied and reported by Bhaskar et al. (2022). Zhou et al. (2016) reported the mechanism of dye degradation on Fenton's oxidation and claimed that organic functional groups are distorted under the action of hydroxyl radicals produced by the dissociation of hydrogen peroxide added.

Psidium gujava, a common tropical plant found in several parts of India, is known for its antimicrobial and anticarcinogenic properties. Rich phenolic compounds such as flavonoids, gallic acid, catechin, and rutin present in the leaves of P. gujava act as a capping and reducing agent in the synthesis of nanoparticles. The potential use of P. gujava for nanoparticles synthesis and characterization has been done by many researchers and synthesized nanoparticles showed better antimicrobial properties (Raghunandan et al. 2009; Khaleel et al. 2010; Parashar et al. 2011). Rashmishree et al. (2022) synthesized and characterized nano iron particles for their application in Fenton's oxidation of triclosan. The interaction of iron and zinc ions in the solution with polyphenols present in the plant extract results in the formation of zinc–iron composites (Devatha et al. 2016; Sangami & Manu 2017). Flavonoids, alkaloids and other chemicals present in the plant extract are essential as reducing and capping agents for the reduction of particle size.

Considering the treatment efficiency and cost-effectiveness of combined adsorption–Fenton's oxidation process, the present study deals with the synthesis of a novel nanocomposite catalyst using bioleached laterite iron (BLFe) and granular activated carbon (GAC) as a precursor and P. gujava plant extract. Catalyst synthesized was evaluated for its catalytic role in Fenton's oxidation process and adsorption studies have been conducted (Bhaskar et al. 2021).

Preparation of P. gujava plant extracts

Fresh leaves of P. gujava were collected from the campus of NITK, Surathkal. Leaves were washed thoroughly with distilled water, dried and cut into small pieces. Cut pieces of leaves were boiled in distilled water at 60–70 °C for 1 h. The extract were filtered and stored for further use at 4 °C.

Phytochemical synthesis of BLFe-based GAC/zinc ferro composites

BLFe was biologically leached out from the laterite soil using the novel acidophilic bacteria Acidithiobacillus ferrooxidans (Bhaskar et al. 2021). BLFe solution of 1 mM concentration and 15 mM zinc solution was added to plant extract at a 1:1 ratio followed by 0.2 g of GAC and mixed thoroughly in the shaker at 200 rpm for 1 h. Solutions were filtered using Whatman's filter paper No. 1 and oven-dried at 105 °C overnight. The extracted particles were stored in moisture-free containers for further use.

BLFe-based GAC/zinc ferro nanocomposites catalyzed Fenton's oxidation of RhB

Oxidative degradation of RhB using BLFe-based GAC/zinc ferro nanocomposites as catalyst was carried out with 10 mg/L of initial dye concentration (Su et al. 2013; Li et al. 2016; Zhou et al. 2016). BLFe-based GAC/zinc ferro nanocomposites were added at an incremental dose into RhB solution in a conical flask. The solution was adjusted to pH 3 using 0.5 M H2SO4 and allowed for 60 min to ensure proper mixing and uniform distribution of BLFe-based GAC/zinc ferro nanocomposites powder in the solution before the addition of H2O2. The investigation was conducted with appropriate experimental conditions by considering different dosages of nanocomposite particles (1.0–10 g/L) and H2O2 quantities (100–1,000 mg/L). Samples were extracted at regular intervals for analysis. During sampling, each time 1 ml of sodium thiosulfate was added to halt the reaction (Khan et al. 2009). The concentration of RhB was measured using a double-beam UV–Vis spectrophotometer at the wavelength of 554 nm (Systronics Make, Model No. AU-2701). Chemical oxygen demand (COD) was measured by the colorimetric method as per 5220D of Standard Methods for Examination of Water and Wastewater (APHA Method 4500-F 1992). pH was measured using a digital pH meter (Model – edge, HANNA Make). Ferrous iron was measured by the 1,10-phenanthroline method using a UV–Vis spectrophotometer at a wavelength of 510 nm (Systronics Make, Model No. AU-2701) (APHA Method 4500-F 1992). Ferric iron was measured by the potassium thiocyanate method using a UV–Vis spectrophotometer at a wavelength of 510 nm (Systronics Make, Model No. AU-2701) (Woods & Mellon 1941). H2O2 was measured using a double-beam UV–Vis spectrophotometer at a wavelength of 470 nm (Systronics Make, Model No. AU-2701) (Eisenberg 1943). A recoverability and reuse test for the spent catalyst was conducted. BLFe-based GAC/zinc ferro nanocomposites powder was filtered, collected, dried and reused as a Fenton's catalyst for the degradation of RhB.

BLFe-based GAC/zinc ferro nanocomposite formation and its characterization

Composites obtained by treating plant extract, zinc–iron solution in addition to GAC were seen as honeycomb structures with clear several pores on the surface with the aid of SEM analysis. Figure 1 presents the SEM images of BLFe-based GAC/zinc ferro composite. Peaks observed with XRD (Figure 2) for GAC/zinc ferro composites at 2Ө 26.69 and 42.23 with d-spacing 3.34 and 2.14 correspond to graphite (PDF: 00-025-0284), peaks at 2Ө 35.64 and 37.70 with d-spacing corresponds to magnetite (PDF: 01-088-0315) and peaks at 2Ө 43.89 with d-spacing 2.06 correspond to iron–zinc (Bhaskar et al. 2021). Table 2 presents the chemical elements by the weight percentage for BLFe-based GAC/zinc ferro nanocomposites. In freshly formed composites, it was observed that BLFe-based GAC/zinc ferro nanocomposites have 65.2% of carbon, 5.7% of iron and 2.7% of zinc contents, respectively (Figure 3). The presence of phosphorous, aluminum and sulfur in minor concentrations are attributed to plant extracts.
Table 2

Chemical composition of BLFe-based GAC/zinc ferro nanocomposites

Elements Fe Zn Al 
Weight (%) 65.2 23.2 5.7 2.7 2.1 0.6 0.6 
Elements Fe Zn Al 
Weight (%) 65.2 23.2 5.7 2.7 2.1 0.6 0.6 
Figure 1

Scanning electron microscopic images of BLFe-based GAC/zinc ferro nanocomposites showing the morphological appearance of synthesized nanoparticles.

Figure 1

Scanning electron microscopic images of BLFe-based GAC/zinc ferro nanocomposites showing the morphological appearance of synthesized nanoparticles.

Close modal
Figure 2

XRD images of BLFe-based GAC/zinc ferro nanocomposites representing the corresponding peaks of synthesized nanoparticles.

Figure 2

XRD images of BLFe-based GAC/zinc ferro nanocomposites representing the corresponding peaks of synthesized nanoparticles.

Close modal
Figure 3

EDS images of BLFe-based GAC/zinc ferro nanocomposites showing the various elements present in the synthesized nanoparticles by percentage weight.

Figure 3

EDS images of BLFe-based GAC/zinc ferro nanocomposites showing the various elements present in the synthesized nanoparticles by percentage weight.

Close modal

BET surface areas were found to be 389 m2/g with a pore volume of 0.51 cm3/g, respectively, confirming the mesoporous structure of the nanoparticles obtained.

Catalytic degradation of RhB by BLFe-based GAC/zinc ferro composites

The degradation of RhB by BLFe-based GAC/zinc ferro nanocomposite catalyzed Adsorption–Fenton's oxidation was investigated (Table 3). Oxidative degradation observed on the addition of H2O2 confirms that the degradation of RhB follows Fenton's reaction. Overall, removal efficiency up to 96.2% was observed with BLFe-based GAC/zinc ferro nanocomposite load of 10.0 g/L and H2O2 dosage of 1,000 mg/L at pH 3 on which initial removal of 31.2% in initial 60 min was attributed to adsorption (Figure 4).
Table 3

Degradation of Rhodamine B on adsorption–Fenton's oxidation process

CatalystDosage of nanocomposites (g/L)H2O2 (mg/L)Rhodamine B degradation (%)COD removal (%)
BLFe-based GAC/zinc ferro nanocomposites 1.0 100 80.3 56.1 
2.0 200 80.5 57.7 
5.0 200 95.0 67.4 
10.0 200 96.2 64.2 
CatalystDosage of nanocomposites (g/L)H2O2 (mg/L)Rhodamine B degradation (%)COD removal (%)
BLFe-based GAC/zinc ferro nanocomposites 1.0 100 80.3 56.1 
2.0 200 80.5 57.7 
5.0 200 95.0 67.4 
10.0 200 96.2 64.2 
Figure 4

Degradation of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites loading with different H2O2 dosage (a) 1.0 g/L GAC/Zn–Fe, (b) 2.0 g/L GAC/Zn–Fe, (c) 5.0 g/L GAC/Zn–Fe and (d) 10.0 g/L GAC/Zn–Fe.

Figure 4

Degradation of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites loading with different H2O2 dosage (a) 1.0 g/L GAC/Zn–Fe, (b) 2.0 g/L GAC/Zn–Fe, (c) 5.0 g/L GAC/Zn–Fe and (d) 10.0 g/L GAC/Zn–Fe.

Close modal

The dosage and form of iron is the prime factor in the Fenton oxidation process (Barbusi & Filipek 2001; Chen et al. 2016). The effect of catalyst dosage was studied by increasing BLFe-based GAC/zinc ferro nanocomposites dosage in the range of 1.0–10.0 g/L. During the study, the degradation of RhB increased with an increase in the load of catalyst. The efficiency of dye removal was observed to increase by 6.7% on increasing catalyst dosage from 1 to 5 mg/L and 7.9% on an increase to 10 mg/L. This observation indicates that BLFe-based GAC/zinc ferro nanocomposites play a catalytic role in the process by decomposing hydrogen peroxide into hydroxyl radicals, thereby accelerating the formation of active sites on the catalyst. Iron leached out of nanocomposites accounts for 0.14 g/L at this stage. A continuous increase in ferric iron concentration was observed during the study.

Maximum decolorization efficiency was observed with 10 g/L of nanocomposites (Figure 5).
Figure 5

Decolorization of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites loading: (a) 1.0 g/L GAC/Zn–Fe – 100 mg/L H2O2, (b) 2.0 g/L GAC/Zn–Fe – 200 mg/L H2O2, (c) 5.0 g/L GAC/Zn–Fe – 200 mg/L H2O2 and (d) 10.0 g/L GAC/Zn–Fe – 200 mg/L H2O2.

Figure 5

Decolorization of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites loading: (a) 1.0 g/L GAC/Zn–Fe – 100 mg/L H2O2, (b) 2.0 g/L GAC/Zn–Fe – 200 mg/L H2O2, (c) 5.0 g/L GAC/Zn–Fe – 200 mg/L H2O2 and (d) 10.0 g/L GAC/Zn–Fe – 200 mg/L H2O2.

Close modal
Total iron leached out of iron particles and involved in the oxidation process is shown in Figure 6(b) with 10.0 g/L of catalyst dosage. The total iron leached into the system was 0.14 g/L with 10.0 g/L of BLFe-based GAC/zinc ferro nanocomposites dosage and 200 mg/L of H2O2 dosage. Iron leached out of nanocomposite is involved in the catalytic action for the dissociation of hydrogen peroxide into hydroxyl ions. This was reported in the previous studies with iron oxide nanoparticles and jarosite as catalysts (Bhaskar et al. 2021, 2022). The ferrous form of iron leached out was oxidized into a ferric form of iron at the initial stage followed by a reversible reaction and precipitation of iron due to hydrolysis. The high oxidation–reduction potential observed during the initial stage of the study is inconsistent with this due to oxidizing environment.
Figure 6

Catalytic degradation of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites loading: (a) iron variation and (b) H2O2 variation.

Figure 6

Catalytic degradation of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites loading: (a) iron variation and (b) H2O2 variation.

Close modal
Figure 4 presents the trend of hydrogen peroxide on dye degradation at different nanocomposite dosages. It is observed that there is a continuous decrease in hydrogen peroxide concentration with time. Dye degradation was increased with an increase in hydrogen peroxide concentration from 100 to 200 mg/L, thereby decreasing the dye removal and marking the optimum dosage. Iron leached out from the nanocomposites initially reacted with H2O2 liberating hydroxyl radicals (Yan et al. 2017). In reusability studies, it was found that dye degradation efficiency was found to have reduced by 27.8% on the usage for five consecutive cycles marking the catalyst re up to five cycles (Figure 7).
Figure 7

Reusability studies of BLFe-based GAC/zinc ferro nanocomposites on Rhodamine B degradation.

Figure 7

Reusability studies of BLFe-based GAC/zinc ferro nanocomposites on Rhodamine B degradation.

Close modal
Adsorption studies reveal that the degradation of RhB using BLFe-based GAC/zinc ferro nanocomposites fits Freundlich Isotherm with a maximum adsorption capacity of 47.8189 mg/g and an R-square value of 0.9819 (Table 4). Li et al. (2022) observed the intermolecular H-bond interaction between iron oxide-based adsorbent for the removal of RhB. The team observed a peak shift in the FTIR results due to the surface interaction between iron oxides and RhB on adsorption (Li et al. 2022). In the present study from the Langmuir isotherm (Figure 8 and Table 5), it is observed that an increase in adsorbent dosage has led to an increase in dye removal efficiency up to 5 g/L of BLFe-based GAC/zinc ferro nanocomposites addition after which the rate of adsorption was observed to be declined. The Freundlich Adsorption Isotherm follows the same trend with a maximum adsorption rate pointing at 5 g/L of BLFe-based GAC/zinc ferro nanocomposites (Figure 9).
Table 4

Freundlich Isotherm model for the degradation of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites

CatalystDosage of nanocomposites (g/L)H2O2 (mg/L)Freundlich Isotherm model
R2
Kf1/n
BLFe-based GAC/zinc ferro nanocomposites 1.0 100 41.1434 1.4585 0.9698 
2.0 200 11.5345 1.2550 0.9677 
5.0 200 47.8189 0.6422 0.9819 
10.0 200 14.7672 0.7579 0.9402 
CatalystDosage of nanocomposites (g/L)H2O2 (mg/L)Freundlich Isotherm model
R2
Kf1/n
BLFe-based GAC/zinc ferro nanocomposites 1.0 100 41.1434 1.4585 0.9698 
2.0 200 11.5345 1.2550 0.9677 
5.0 200 47.8189 0.6422 0.9819 
10.0 200 14.7672 0.7579 0.9402 
Table 5

Langmuir Adsorption Isotherm model for the degradation of Rhodamine B with BLFe-based GAC/zinc ferro nanocomposites

CatalystDosage of nanocomposites (g/L)H2O2 (mg/L)Langmuir Isotherm Model
R2
K (l/mg)Qmax (mg/g)
BLFe-based GAC/zinc ferro nanocomposites 1.0 100 0.4134 16.29 0.8646 
2.0 200 0.4208 19.01 0.9001 
5.0 200 0.6746 39.21 0.9235 
10.0 200 0.6598 19.45 0.9017 
CatalystDosage of nanocomposites (g/L)H2O2 (mg/L)Langmuir Isotherm Model
R2
K (l/mg)Qmax (mg/g)
BLFe-based GAC/zinc ferro nanocomposites 1.0 100 0.4134 16.29 0.8646 
2.0 200 0.4208 19.01 0.9001 
5.0 200 0.6746 39.21 0.9235 
10.0 200 0.6598 19.45 0.9017 
Figure 8

Linear Langmuir Adsorption Isotherm model for BLFe-based GAC/zinc ferro nanocomposites with (a) 1.0 g/L GAC/Zn–Fe – 100 mg/L H2O2, (b) 2.0 g/L GAC/Zn–Fe – 200 mg/L H2O2, (c) 5.0 g/L GAC/Zn–Fe – 200 mg/L H2O2 and (d) 10.0 g/L GAC/Zn–Fe – 200 mg/L H2O2.

Figure 8

Linear Langmuir Adsorption Isotherm model for BLFe-based GAC/zinc ferro nanocomposites with (a) 1.0 g/L GAC/Zn–Fe – 100 mg/L H2O2, (b) 2.0 g/L GAC/Zn–Fe – 200 mg/L H2O2, (c) 5.0 g/L GAC/Zn–Fe – 200 mg/L H2O2 and (d) 10.0 g/L GAC/Zn–Fe – 200 mg/L H2O2.

Close modal
Figure 9

Linear Freundlich Adsorption Isotherm model for BLFe-based GAC/zinc ferro nanocomposites with (a) 1.0 g/L GAC/Zn–Fe – 100 mg/L H2O2, (b) 2.0 g/L GAC/Zn–Fe – 200 mg/L H2O2, (c) 5.0 g/L GAC/Zn–Fe – 200 mg/L H2O2 and (d) 10.0 g/L GAC/Zn–Fe – 200 mg/L H2O2.

Figure 9

Linear Freundlich Adsorption Isotherm model for BLFe-based GAC/zinc ferro nanocomposites with (a) 1.0 g/L GAC/Zn–Fe – 100 mg/L H2O2, (b) 2.0 g/L GAC/Zn–Fe – 200 mg/L H2O2, (c) 5.0 g/L GAC/Zn–Fe – 200 mg/L H2O2 and (d) 10.0 g/L GAC/Zn–Fe – 200 mg/L H2O2.

Close modal

It is the high redox active metal ions that contribute to more redox reactions by increasing the oxidation property in zinc-doped ferro nanocomposites leading to a higher removal rate compared with other nanocomposites (Nair & Kurian 2017). The adsorption capacity of different materials for the removal of RhB is presented in Table 6. It is observed from the previous studies that sodium montmorillonite acts as a good adsorbent with an adsorption capacity of 35.45 m2/g (Selvam et al. 2008).

Table 6

Adsorption capacity of different adsorbents

AdsorbentQmaxBET (m2/g)Surface morphology/Mineral compositionReference
Titania silica 0.11 272.38 Lamellar, granular  
Coal ash 2.86 8.4 Quartz, mullite, hematite  
Sodium montmorillonite 38.27 35.45 – Selvam et al. (2008)  
BLFe-based GAC/zinc ferro nanocomposites 39.21 389.0 Honeycomb structures with clear several pores on the surface The present study 
AdsorbentQmaxBET (m2/g)Surface morphology/Mineral compositionReference
Titania silica 0.11 272.38 Lamellar, granular  
Coal ash 2.86 8.4 Quartz, mullite, hematite  
Sodium montmorillonite 38.27 35.45 – Selvam et al. (2008)  
BLFe-based GAC/zinc ferro nanocomposites 39.21 389.0 Honeycomb structures with clear several pores on the surface The present study 

Phytochemical synthesis of green synthesis of BLFe-based GAC/zinc ferro nanocomposites led to the formation of honeycomb-like nanocomposites. The presence of iron and zinc was confirmed with EDS and XRD studies. Synthesized nanocomposites exhibited a catalytic role in the Fenton's oxidation along with surface adsorption contributing maximum dye removal of 96.2% within 200 min of treatment. COD removal of about 64.2% observed within 40 min of treatment indicates better oxidation during the treatment. Adsorption studies suggest the Freundlich Adsorption Isotherm model with maximum adsorption. Recoverability and reusability studies suggest that nanocomposites can be reused effectively for up to five consecutive cycles for the removal of RhB dye.

The authors have consent to publish this article.

All authors contributed to the study's conception and analysis. Material preparation and design were performed by S.B., R.K.N., B.M. and M.Y.S. Analysis was carried out by S.B. and R.K.N. The first data of the manuscript was written by S.B. and all authors commented on previous versions of the manuscript. All authors read and approved the final manuscript.

No funding was received for conducting this study.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

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