Heterogeneous Activation of Persulfate by LaMO 3 (M=Co, Fe, Cu, Mn, Ni) Perovskite Catalysts for the Degradation of Organic Compounds

: Sulfate radical-based advanced oxidation processes (SR-AOPs) are lately applied for the degradation of various pollutants through the formation of reactive oxidant species (ROS) from activation of oxidants, such as persulfate (PS) or peroxymonosulfate (PMS). In this study, LaMO 3 (M=Co, Fe, Cu, Mn, Ni) perovskite catalysts were synthesized, characterized by several techniques, and tested for the activation of persulfate towards the degradation of phenolic pollutants. The effect of substitution of position B of La-based perovskites as well as calcination temperature was studied. Overall, the results showed that the decisive role in the catalytic activity was the presence of structures that enhance the transfer of electrons between perovskite and oxidant. LaNiO 3 followed by LaCoO 3 were found as the most active catalysts. Finally, the stability of the catalysts was studied, showing that B-metal leaching is signiﬁcant for both catalysts, with LaCoO 3 being the most stable one.


Introduction
Since water resources' pollution is one of the major environmental problems in recent years, environmental and chemical technology is moving towards the development of novel and effective decontamination technologies [1]. This need lies in the fact that most emerging organic pollutants, such as pharmaceuticals, antibiotics, pesticides, etc., are resistant, toxic, and exhibit low biodegradability. As a result, it is practically difficult degrade them with conventional methods [2][3][4]. As effective methods of decontamination of water and wastewater, advanced oxidation processes (AOPs) are widely applied for the degradation of various resistant pollutants through the formation of reactive oxidant species (ROS), such as hydroxyl ( • OH) or sulfate radicals (SO 4 •− ) [5]. A wide variety of AOPs, such as electrochemical [6], photochemical [7], sonochemical [8], photocatalytic, and catalytic processes [9], can be used for the formation of ROS. These processes may differ both in the way in which ROS are formed as well as in the ROS formed. Nevertheless, they can achieve complete or partial degradation of the pollutants in degradation products of much lower toxicity compared to the original ones [10]. Lately, sulfate radical-based advanced oxidation processes (SR-AOPs) are applied for the degradation of various resistant pollutants through the activation of oxidants, such as persulfate (PS) or peroxymonosulfate (PMS), for the formation of ROS [11]. The formation of sulfate radicals is of particular interest to the scientific community, mainly because of the advantages they exhibit over hydroxyl radicals. Some of the main disadvantages of the decontamination methods based on • OH radicals are the limited pH range (2)(3)(4) and the creation of sludge in the case of photo-Fenton process [12] and generally the shorter half-life of • OH radicals [13].
In this paper, we focus on the synthesis by the surfactant combustion method of a series of lanthanum-based perovskites with different metal ions in position B of the perovskite structure (LaMO 3 , M=Co, Fe, Cu, Mn, Ni). The synthesized perovskites were characterized by several techniques, and their catalytic activity in terms of the degradation of phenolic compounds by activation of PS was subsequently studied. In the catalytic activity experiments, phenol was used as a standard pollutant, as it belongs to a class of compounds that not only shows high levels of toxicity and has harmful effects on the human body but also on that of animals [45]. In addition, for the most active material, the effect of the calcination temperature during the synthetic method on the catalytic activity was also studied.

Characterization of LaMO 3
The x-ray diffraction patterns of synthesized perovskite materials are presented in Figure 1. First, diffractograms of LaMnO 3 and LaFeO 3 materials show the formation of well crystalline perovskite structures with LaFeO 3 presenting orthorhombic phase while LaMnO 3 presents triangular and cubic perovskite phase. These findings are in agreement with analogous materials synthesized by Rao et al. 2018 [46] and Zhang et al. 2018 [47] for LaFeO 3 and Wang et al. 2019b [48] for LaMnO 3 although different synthesis approaches have been used, i.e., sol-gel citric acid method for LaFeO 3 and hydrothermal-PVP method for LaMnO 3 . For LaCoO 3 , LaNiO 3 , and LaCuO 3 , the diffractograms showed a diversity in the crystalline phases formed. LaCoO 3 presented three phases, with perovskite monoclinic structure being the more abundant one, followed by orthorhombic perovskite Ruddlesden-Popper (RP) structure and cobalt oxide with cubic structure. In the cases of Hammouda et al. 2017 [49] and Guo et al. 2020 [50], where citric acid sol-gel method was used, cubic and rhombohedral structures occurred, respectively. LaNiO 3 also presents three phases, with a greater percentage of orthorhombic RP and smaller percentages of homologous perovskite structure with orthorhombic structure and oxide with triangular structure. In the case of synthesized perovskite with citric acid sol-gel method [40], a cubic structure is reported. LaCuO 3 consists of two phases, the main one being orthorhombic RP and, in a smaller percentage, monoclinic oxide, while in the case of Lin et al. (2017) [43], where glycine-combustion preparation method was followed, peaks corresponding to oxides are presented to a small extent, and the main structure corresponds to the rhombohedral structure. Based on the XRD diagram, LaCuO 3 perovskite exhibits a higher crystallinity degree as compared to the other catalysts. Finally, for the LaNiO 3 material that was also calcined at 800 • C (LaNiO 3 -800), it was found that the Ruddlesden-Popper perovskite structure decreased, and the largest percentage is found in the classical ABO 3 structure. Table 1 shows details of the crystalline phases, as identified by the Match program. The RP designation next to the phases corresponds to RP-perovskite from the Ruddlesden-Popper homologous perovskite series. Nitrogen adsorption-desorption isotherms at 77 K for all studied materials are shown in Figure 2. For LaMnO 3, LaFeO 3, LaCoO 3 , and LaNiO 3 , the isotherms obtained are of type IV with a hysteresis loop of type H2(b) according to IUPAC classification [51] corresponding to mesoporous materials. The specific surface area ranged from 7 m 2 /g for LaCoO 3 to 14 m 2 /g for LaFeO 3 , which is a similar range to several perovskites in the literature [50,52] although there are also cases where synthesized perovskites display specific surface areas in the order of 60-120 m 2 /g [53,54], while the respective pore diameters were 18.4 Å and 88.9 Å. On the other hand, LaCuO 3 and LaNiO 3 -800 materials appear as non-porous and adsorption-desorption isotherms are of type II with H2(b) type hysteresis loop. Their specific surface areas display values of 7 m 2 /g and 5 m 2 /g, respectively. Hydrodynamic particle sizes have been also measured by dynamic light scattering (DLS). Median particle diameters were 0.221, 0.250, 0.288, 0.392, and 2.018 µm for LaNiO 3 , LaMnO 3 , LaFeO 3 , LaCoO 3 , and LaCuO 3 , respectively.
Scanning electron microscopy (SEM) was used to reveal the morphology of synthesized perovskites. Based on the microphotographs from all samples for various magnifications (Figure 3), it was observed that none of the materials show a clear geometric crystalline shape. LaMnO 3 appears to have a uniform spongy texture, and LaFeO 3 appears to have a partly spongy texture, while its surface appears to be rougher than LaMnO 3 . Moreover, LaCoO 3 , is also partly spongy, but the interstices between them appear to be more spaced than in the previous cases. The above texture characteristics are consistent with results reported elsewhere [40]. LaNiO 3 appears to exhibit a spongy texture as well, which was retained after calcination to 800 • C. LaCuO 3 seems to be more "fragmented," while at the same time, there are larger aggregates in size, and the expected interstices that would make it spongy are not observed.

Effect of B-position Metal Ion and Calcination Temperature
According to Figure 4, depending on the metal cation that occupies the B position of each perovskite catalyst, a significant differentiation was observed in the degradation rate of phenolics. The catalytic activity followed the trend: LaNiO 3 > LaCoO 3 > LaCuO 3 > LaMnO 3 > LaFeO 3 , with the corresponding rate constants of 0.082 min −1 , 0.029 min −1 , 0.006 min −1 , 0.0009 min −1 , and 0.00004 min −1 (Table 2). Apparently, there is no correlation between the specific surface area of perovskites and their catalytic activity. On the other hand, the presence of two different oxidation states of the metal in position B in the structure of perovskites appears to play a decisive role in their catalytic activity, making easier electron transfer processes between the surface of the perovskites and the oxidant, as it has been reported also elsewhere [42]. For example, in the case of LaCuO 3 (La 2 CuO 4 -RP-orthorombic 80%), it has been reported that copper is present as Cu(I) and Cu(II) [55]. In addition, RP-perovskite structures showed excellent variability in lattice oxygen and charge-transfer ability. The co-presence of RP and single-perovskite structure was demonstrated to exhibit superior activity for phenol degradation as compared to pure-phase perovskite materials. The higher activity was attributed to the higher amount of generated oxygen vacancies, the stronger affinity of perovskite surface to the reactants (PMS and phenol), and the higher electron conduction efficiency [56]. In consistency, the catalysts presenting mixed RP and single-perovskite structures were the more efficient ones in the present study.    Since LaNiO 3 was the most active material in terms of phenolic degradation, the effect of calcination temperature was studied at a higher calcination temperature 800 • C (vs. 600 • C). As can be seen in Figure 4, the catalytic activity of LaNiO 3 -800 is reduced compared to that calcined at 600 • C. The increase in calcination temperature led to a material that retained its original spongy structure but with a lower specific surface area, the lowest of all previous materials, and a significant variation of the % phase content, with single-LaNiO 3 phase prevailing. As a result, the ratio of RP to single-perovskite structure plays a significant role in the catalytic efficiency. However, LaNiO 3 -800 is still more active than all the other materials with a different B-cation, which reinforces the consideration that crystal phase ratio and the co-current presence of phases with different oxidation states of B-metal is the crucial parameter affecting the activity. Table 3 summarizes previous data for phenol degradation through persulfate activation with perovskite catalysts. For comparison to the most active materials presented in this research, it should be taken into consideration the different method of substrate determination. The previous studies [56][57][58][59] monitored the degradation of initial phenol concentration by HPLC, while the current method monitored the removal of the total phenolic content (phenol plus phenolic transformation products formed during the process). LaCoO 3 displays comparable efficiency (k = 0.029 min −1 ) to the lower values reported among the other materials. On the other hand, LaNiO 3 displays the second best rate constant (0.082 min −1 ) ( Table 3). Three different scavengers were used in order to elucidate the degradation mechanism and the dominant ROS generated during the treatment. Tert-butanol (TBA), which does not contain α-hydrogens, was used as a scavenger for the generated • OH, as it reacts rapidly with the produced hydroxyl radicals. Ethanol (EtOH), which contains α-hydrogens, was used as scavenger for both hydroxyl and sulfate radicals [60], and NaN 3 was used as a scavenger for both • OH and SO 4 •− radicals as well as singlet oxygen ( 1 O 2 ) [61]. Since the predominance of the synthetic method with the calcination temperature at 600 • C versus 800 • C was presented, the materials that will be studied in terms of the degradation mechanism of phenolics are the most active of this series, namely LaCoO 3 and LaNiO 3 .
As mentioned above, in the case of the LaCoO 3 /PS system, phenol degradation of 96% was observed in just 90 min, with a corresponding rate constant of 0.029 min −1 . In the presence of both TBA and EtOH, a minimal decrease in phenol degradation was observed, as shown by the Figure 5a, to 89% and 87% over 90 min, respectively, which means that the formation of • OH contributes in a greater percentage to the degradation of phenolics and, in a smaller percentage, of SO 4 •− . However, in the case when NaN 3 was used as a scavenger, a decrease in phenolic degradation was observed to a greater extent. Particularly, a decrease in phenol degradation was observed from 96% in the absence of a scavenger to 82% in 90 min, with the corresponding rate constant decreasing from 0.029 min −1 to 0.015 min −1 . Thus, in the LaCoO 3 /PS system, 1 O 2 and • OH had a greater contribution to the degradation of phenolics while SO 4 •− were formed in a minor amount. Additionally, in the case of the LaNiO 3 /PS system, as can be seen from the Figure 5b, the inhibition in the presence of azide ions predominates since there is a decrease in the degradation of phenolics from 96% (k = 0.082 min −1 ) in the absence of a scavenger to 71% (0.030 min −1 ) within 30 min. A significant decrease is also observed in the cases where TBA and EtOH were used as scavengers. Specifically, in the case of EtOH, there was a decrease in phenol degradation to 76% in 30 min, with the corresponding rate constant of 0.042 min −1 , while in the case of TBA, there was a decrease to 86% in 30 min with the rate constant of 0.053 min −1 . This means that all the three ROS, namely 1 O 2 , • OH, and SO 4 •− , were formed and contributed the degradation of phenolics.

Reusability and Stability of the Best Catalysts
The stability-reusability of LaCoO 3 and LaNiO 3 catalysts for three catalytic cycles was studied ( Figure 6). In the LaCoO 3 /PS system, it is evident that the catalyst performance is not affected after three catalytic cycles. In the first two cycles, the degradation of phenol remained stable at 96%, while in the third cycle, there was a slight decrease at 89%. However, this is not observed in the case of the LaNiO 3 /PS system, as there is a gradual decrease in the catalytic activity of perovskite, i.e., from 96% in the first cycle to 90% in the second cycle, followed by a greater decrease in the third cycle, down to 58%.
Particularly, a decrease in phenol degradation was observed from 96% in the absence of a scavenger to 82% in 90 min, with the corresponding rate constant decreasing from 0.029 min −1 to 0.015 min −1 . Thus, in the LaCoO3/PS system, 1 O2 and • OH had a greater contribution to the degradation of phenolics while SO4 •− were formed in a minor amount. Additionally, in the case of the LaNiO3/PS system, as can be seen from the Figure 5b, the inhibition in the presence of azide ions predominates since there is a decrease in the degradation of phenolics from 96% (k = 0.082 min −1 ) in the absence of a scavenger to 71% (0.030 min −1 ) within 30 min. A significant decrease is also observed in the cases where ΤΒΑ and ΕtΟΗ were used as scavengers. Specifically, in the case of ΕtΟΗ, there was a decrease in phenol degradation to 76% in 30 min, with the corresponding rate constant of 0.042 min −1 , while in the case of TBA, there was a decrease to 86% in 30 min with the rate constant of 0.053 min −1 . This means that all the three ROS, namely 1 O2, • OH, and SO4 •− , were formed and contributed the degradation of phenolics. Metal leaching was studied as well in order to correlate with the reusability of the catalysts since gradual metal release leads to their deactivation [62]. As observed in Figure 7, there is a gradual increase with a rather constant rate in the amount of cobalt lost from LaCoO 3 perovskite, with the total concentration after the third cycle being approximately 6.6 mgL −1 . In the case of LaNiO 3 , higher concentrations of nickel ion were detected, i.e., 14.39 mgL −1 for the first cycle to 17.24 mgL −1 for the third cycle. The subsequent gradual increase in the metal losses after each catalytic cycle has been reported to affect the surface properties of perovskites and thus explains the corresponding decrease in their catalytic activity [50]. Metal leaching in these cases can be due to two reasons: either the existence of even a small degree of water solubility of the catalyst (due to the oxides of the metals they may contain) [63] or the formation of water-soluble products that can result from the reaction of the catalyst with the solvent-oxidant system [64]. Thus, comparing these two materials in terms of their stability, the prevalence of LaCoO 3 over LaNiO 3 is significant.

Reusability and Stability of the Best Catalysts
The stability-reusability of LaCoO3 and LaNiO3 catalysts for three catalytic cycles was studied ( Figure 6). In the LaCoO3/PS system, it is evident that the catalyst performance is not affected after three catalytic cycles. In the first two cycles, the degradation of phenol remained stable at 96%, while in the third cycle, there was a slight decrease at 89%. However, this is not observed in the case of the LaNiO3/PS system, as there is a gradual decrease in the catalytic activity of perovskite, i.e., from 96% in the first cycle to 90% in the second cycle, followed by a greater decrease in the third cycle, down to 58%. Metal leaching was studied as well in order to correlate with the reusability of the catalysts since gradual metal release leads to their deactivation [62]. As observed in Figure 7, there is a gradual increase with a rather constant rate in the amount of cobalt lost from LaCoO3 perovskite, with the total concentration after the third cycle being approximately 6.6 mgL −1 . In the case of LaNiO3, higher concentrations of nickel ion were detected, i.e., 14.39 mgL −1 for the first cycle to 17.24 mgL −1 for the third cycle. The subsequent gradual increase in the metal losses after each catalytic cycle has been reported to affect the surface properties of perovskites and thus explains the corresponding decrease in their catalytic activity [50]. Metal leaching in these cases can be due to two reasons: either the existence of even a small degree of water solubility of the catalyst (due to the oxides of the metals they may contain) [63] or the formation of water-soluble products that can result from the reaction of the catalyst with the solvent-oxidant system [64]. Thus, comparing these two materials in terms of their stability, the prevalence of LaCoO3 over LaNiO3 is significant.

Synthetic Method of LaMO 3
The synthesis of perovskites was carried out in the presence of the anionic surfactant glycolic acid ethoxylate lauryl ether. Initially, 100 mL of 0.05 M solution of anionic surfactant were stirred for 10 min at 25 • C, 1N HNO 3 was added to adjust the pH = 1.00, and then, the solution was stirred for 1h. Then, determined volumes of 0.05 M La(NO 3 ) 3 × 6H 2 O were added, and the mixture was left under stirring for 1h. Afterwards, determined volumes of the corresponding metal nitrate hydrate reagents was added and stirred for 24 h. Finally, the obtain solids were dried at 90 • C and then calcinated at 600 • C for 6 h under atmospheric conditions. Best catalyst (LaNiO 3 ) was also calcined at 800 • C for comparison in the catalytic activity.

Characterization of LaMO 3
X-ray diffraction (XRD) patterns of the synthesized materials were obtained using a D8 Bruker Advance diffractometer with a monochromatic radiation Cu-Ka (λ = 1.5406 Å) in the scanning range 10 • ≤ 2θ ≤ 90 • and scanning rate of 0.01 • /s. The samples were measured in powder form after they were calcined. Identification of crystal phases was carried out via the trial version of Match! 3 Software (Crystal impact, Bonn, Germany).
The surface area of the synthesized materials was measured by adsorption-desorption N 2 . Adsorption-desorption isotherms were obtained with the Autosorb-1 porosimeter at a liquid nitrogen temperature of 77 K, using a 9-mm measuring cell with the corresponding rod. Degassing of materials at 180 • C for 5 h was required before the measurement. The surface morphology of the particles was observed in a Jeol JSM 5600 system operating at 20 kV. Prior to the analysis, the solids were sputtered with gold under argon atmosphere. A Shimadzu SALD-2300 laser diffraction particle size analyzer (Kyoto, Japan) working with dynamic light scattering (DLS) mode was used for the hydrodynamic particle size measurements.

Catalytic Activity of LaMO 3 Materials
Phenolics degradation experiments were carried out in 200-mL conic flasks containing 100 mL of phenol aquatic solution with an initial concentration of 10 mgL −1 and specific amounts of catalyst (LaMO 3 ) under continuous stirring, at room temperature. In order to start the reaction, oxidant (sodium persulfate) was added into the reactor. Then, at predetermined time intervals, 6 mL of the reaction solution were withdrawn, quenched immediately with methanol to terminate the oxidation reaction, and filtered by 0.45-µm membrane filter. Finally, 5 mL of the collected sample were used for the determination of phenolics concentration by Folin-Ciocalteu method [65] using a UV/Vis spectrophotometer (V-360, Jasco, Tokyo, Japan). The reusability of the catalysts with the best activity was studied through catalytic cycle experiments following the previous procedures. At the end of each catalytic cycle, the catalyst was collected and rinsed with distilled water. The stability of the best catalysts was also studied by determining the concentration of the leached B metals (Co, Ni) at the end of each catalytic cycle, utilizing ICP-MS/Laser Ablation technique. The analysis was performed using a NWR213 laser ablation system (Elemental Scientific, Omaha, NE, USA) attached to an iCAP Q-ICP-MS unit (Thermo Scientific, Waltham, MA, USA).

Conclusions
The choice of the metal ion at position B of the perovskite structure appears to significantly affect the properties of the synthesized perovskites, including both their surface properties and the catalytic activity. Of the series of perovskites synthesized, the most active for persulfate activation and subsequent degradation of phenolics was LaNiO 3 followed by LaCoO 3 . The co-presence of RP and single-perovskite structure was demonstrated to exhibit superior activity. Still, it was shown that the increase in calcination temperature resulted in lower catalytic activity. Finally, the use of LaCoO 3 and LaNiO 3 for consecutive catalytic cycles revealed better recyclability and lower metal leaching for LaCoO 3 . Further techniques aiming at diminishing metal losses should be considered in future research.