Preparation of Porous Ti/RuO2-IrO2@Pt, Ti/RuO2-TiO2@Pt and Ti/Y2O3-RuO2-TiO2@Pt Anodes for Efficient Electrocatalytic Decomposition of Tetracycline

Electrocatalytic oxidation (ECO) has attracted attention because of its high efficiency and environmental friendliness in water treatment. The preparation of anodes with high catalytic activity and long service lifetimes is a core part of electrocatalytic oxidation technology. Here, porous Ti/RuO2-IrO2@Pt, Ti/RuO2-TiO2@Pt, and Ti/Y2O3-RuO2-TiO2@Pt anodes were fabricated by means of modified micro-emulsion and vacuum impregnation methods with high porosity titanium plates as substrates. The scanning electron microscopy (SEM) images showed that RuO2-IrO2@Pt, RuO2-TiO2@Pt, and Y2O3-RuO2-TiO2@Pt nanoparticles were coated on the inner surface of the as-prepared anodes to form the active layer. Electrochemical analysis revealed that the high porosity substrate could result in a large electrochemically active area, and a long service life (60 h at 2 A cm−2 current density, 1 mol L−1 H2SO4 as the electrolyte, and 40 °C). The degradation experiments conducted on tetracycline hydrochloride (TC) showed that the porous Ti/Y2O3-RuO2-TiO2@Pt had the highest degradation efficiency for tetracycline, reaching 100% removal in 10 min with the lowest energy consumption of 167 kWh kg−1 TOC. The reaction was consistent with the pseudo-primary kinetics results with a k value of 0.5480 mol L−1 s−1, which was 16 times higher than that of the commercial Ti/RuO2-IrO2 electrode. The fluorospectrophotometry studies verified that the degradation and mineralization of tetracycline were mainly ascribed to the •OH generated in the electrocatalytic oxidation process. This study thus presents a series of alternative anodes for future industrial wastewater treatment.


Introduction
Tetracycline hydrochloride (TC) is a typical broad-spectrum antibiotic that is widely used in treating infectious diseases of humans and livestock [1,2]. The production and consumption amount of tetracycline are more than several tens of thousands of tons per year, which makes it one of the most widely detected antibiotics in the world at the levels of mg L −1 in soil and ng L −1 -µg L −1 in natural water [3,4]. Furthermore, tetracycline has persistently existed in the aquatic ecosystem, and it is difficult to metabolize in the microbial system, which represents a long-term threat to human health and the ecological environment [5][6][7]. Therefore, dealing with the tetracycline pollution problem has become an increasingly prominent issue. Several studies have been carried out in the past decades to develop efficient methods for tetracycline degradation, such as adsorption [8][9][10], membrane separation [11], chemical oxidation [12], etc.
Recently, advanced oxidation technology (AOT) (e.g., Fenton oxidation, ozonation, photocatalysis, and electrocatalytic oxidation) has been applied as a primary chemical oxidation method in many water treatment plants due to its strong oxidation capability [10]. Among the available AOTs, electrocatalytic oxidation (ECO) is recognized as a highly

Morphological and Structural Characterization
The morphology of the prepared porous Ti/RuO 2 -IrO 2 @Pt, Ti/RuO 2 -TiO 2 @Pt, and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt anodes were characterized via SEM and EDS. As shown in Figure 1a-c, the surface structure was apparently changed after coating with RuO 2 -IrO 2 @Pt, RuO 2 -TiO 2 @Pt, and Y 2 O 3 -RuO 2 -TiO 2 @Pt composites. The precursor solution was filled in the inner pores of the porous Ti plate and coated on the surface of Ti particles. The pore structure was analyzed by means of the injection of mercury, as shown in Figure S2 and Table S1, and the mercury intrusion pore size distribution further indicated that the inner pores were filled, since the average pore size was reduced from 24.47 µm to 10.89 µm, 14.84 µm, and 12.64 µm, respectively, after coating with the RuO 2 -IrO 2 @Pt, RuO 2 -TiO 2 @Pt, and Y 2 O 3 -RuO 2 -TiO 2 @Pt composites. In contrast, the total pore capacity and total pore area were increased after coating, which can probably be ascribed to the microstructure of the composite coating layer. Additionally, compared with Ti/RuO 2 -TiO 2 @Pt, Ti/RuO 2 -IrO 2 @Pt, and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt, the anodes showed a much smoother surface with very few defects, which may lead to a much more stable performance in the ECO process [31][32][33]. The EDS mapping ( Figure S3) showed that for the prepared porous Ti/RuO 2 -IrO 2 @Pt, Ti/RuO 2 -TiO 2 @Pt, and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt anodes, the elements of Ru, Pt, Ti, and Y were uniformly distributed on the electrode surface. The chemical structure of the anodes was characterized using XRD spectroscopy (Figure 1d). According to the Joint Committee on Powder Diffraction Standards (JCPDS) card, the main diffraction peaks identified near 28 • , 35 • , and 54 • were ascribed to RuO 2 (JCPDS 88-0323)-based mixed oxides with IrO 2 (JCPDS 86-0330), PtO 2 (JCPDS 75-1059), or TiO 2 (JCPDS 88-1175). The peak that appeared at 46.3 • corresponded to Pt 0 (JCPDS 04-0802). Identified using the microemulsion method, Pt 0 could be held in the composite, and this probably led to an enhancement in the electron transfer capability and resulted in efficient performance in the ECO process [34][35][36][37].

Electrochemical Performance Analysis
The electrochemical performance of each anode was tested via the linear sweep voltammetry (LSV) technique using a three-electrode system with 1.0 M KOH electrolytes [38][39][40]. The collected LSV polarization curves are shown in Figure 2a. We discovered that

Electrochemical Performance Analysis
The electrochemical performance of each anode was tested via the linear sweep voltammetry (LSV) technique using a three-electrode system with 1.0 M KOH electrolytes [38][39][40]. The collected LSV polarization curves are shown in Figure 2a. We discovered that the addition of Pt in the composites could enhance its activity in the oxygen evolution reaction (OER), which resulted in lower potentials of~0.38 V for Ti/RuO 2 -TiO 2 @Pt,~0.44 V for Ti/RuO 2 -IrO 2 @Pt, and~0.49 V for Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt (vs. SCE), respectively, compared with that of the commercial Ti/RuO 2 -IrO 2 electrode. In addition, the kinetics of the anodes for OER were investigated through the Tafel plot ( Figure 2b). The Tafel slope of commercial Ti/RuO 2 -IrO 2 was 469.83 mV dec −1 , whereas those of the porous Ti/RuO 2 -TiO 2 @Pt, Ti/RuO 2 -IrO 2 @Pt, and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt were 417.46, 425.98, and 446.78 mV dec −1 , respectively. There was not much of a difference among the Tafel slope values of the electrodes, which could be due to the fact that the main component of all the electrodes was RuO 2 , and this had the main influence on the kinetics of the anodes for OER. ECSA analysis was performed to evaluate the catalytic activity of the prepared electrodes in the ECO reaction. Cyclic voltammetry (CV) curves were obtained at scan rates from 10 to 60 mV s −1 in a non-Faraday section for the calculation of double-layer capacitance (C dl ) values [41,42]. The C dl values had a positive correlation with the ECSA results of the electrodes. As shown in Figure 2c, the calculated C dl value of porous Ti/RuO 2 -IrO 2 @Pt was 269.2 mF cm −2 , which was 5.4 times higher than that of commercial Ti/RuO 2 -IrO 2 electrodes. This result indicated that the porous Ti substrate could substantially increase the ECSA of the electrodes, which led to an increase in the number of revelational active sites and boosted their electrical catalytic activity in the ECO reactions. In addition, accelerated life testing was conducted in 1 M H 2 SO 4 solution at 2 A cm −2 to assess the stability of the electrodes [43]. We observed that the commercial Ti/RuO 2 -IrO 2 electrode only held for 1475 min, whereas the porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt and Ti/RuO 2 -IrO 2 @Pt electrodes lasted 3576 and 3588 min, respectively, which were twice as high as that of the commercial Ti/RuO 2 -IrO 2 electrode (Figure 2d). This shows that the porous electrode surface structure was dense and the electrocatalytic layer formed was more stable, which effectively prevented the corrosion of the electrolyte and enhanced the service life of the electrode.
the addition of Pt in the composites could enhance its activity in the oxygen evolution reaction (OER), which resulted in lower potentials of ~0.38 V for Ti/RuO2-TiO2@Pt, ~0.44 V for Ti/RuO2-IrO2@Pt, and ~0.49 V for Ti/Y2O3-RuO2-TiO2@Pt (vs. SCE), respectively, compared with that of the commercial Ti/RuO2-IrO2 electrode. In addition, the kinetics of the anodes for OER were investigated through the Tafel plot ( Figure 2b). The Tafel slope of commercial Ti/RuO2-IrO2 was 469.83 mV dec −1 , whereas those of the porous Ti/RuO2-TiO2@Pt, Ti/RuO2-IrO2@Pt, and Ti/Y2O3-RuO2-TiO2@Pt were 417.46, 425.98, and 446.78 mV dec −1 , respectively. There was not much of a difference among the Tafel slope values of the electrodes, which could be due to the fact that the main component of all the electrodes was RuO2, and this had the main influence on the kinetics of the anodes for OER. ECSA analysis was performed to evaluate the catalytic activity of the prepared electrodes in the ECO reaction. Cyclic voltammetry (CV) curves were obtained at scan rates from 10 to 60 mV s −1 in a non-Faraday section for the calculation of double-layer capacitance (Cdl) values [41,42]. The Cdl values had a positive correlation with the ECSA results of the electrodes. As shown in Figure 2c, the calculated Cdl value of porous Ti/RuO2-IrO2@Pt was 269.2 mF cm −2 , which was 5.4 times higher than that of commercial Ti/RuO2-IrO2 electrodes. This result indicated that the porous Ti substrate could substantially increase the ECSA of the electrodes, which led to an increase in the number of revelational active sites and boosted their electrical catalytic activity in the ECO reactions. In addition, accelerated life testing was conducted in 1 M H2SO4 solution at 2 A cm −2 to assess the stability of the electrodes [43]. We observed that the commercial Ti/RuO2-IrO2 electrode only held for 1475 min, whereas the porous Ti/Y2O3-RuO2-TiO2@Pt and Ti/RuO2-IrO2@Pt electrodes lasted 3576 and 3588 min, respectively, which were twice as high as that of the commercial Ti/RuO2-IrO2 electrode ( Figure 2d). This shows that the porous electrode surface structure was dense and the electrocatalytic layer formed was more stable, which effectively prevented the corrosion of the electrolyte and enhanced the service life of the electrode.

Effect of Electrolyte Type and Concentration
Testing of the degradation of tetracycline with NaCl and Na 2 SO 4 electrolyte solutions was conducted to evaluate the effect of electrolytes on the electrocatalytic oxidation of tetracycline [44]. As shown in Figure 3, for all the electrodes, the tetracycline degradation efficiency of NaCl as an electrolyte was much higher than that of Na 2 SO 4 . This can probably be ascribed to the fact that Cl − ions in the solution could be oxidized, generating •Cl, HClO, and other reactive chlorine species, which could further react with tetracycline molecules or by-products to enhance the tetracycline degradation efficiency [45]. In addition, the effect of the NaCl concentration on the degradation of tetracycline was also studied ( Figure 3). As presented in the inserts of Figure 3d-f, the kinetics under different NaCl concentrations were consistent with pseudo-first-order kinetics. For porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt, the calculated k value increased with increasing NaCl concentration and reached the maximum value of 0.55 min −1 at an NaCl concentration of 3.5 g L −1 . Meanwhile, 38.2% TOC removal was achieved in a 20 min reaction time, accompanied by an EC of 167 kWh kg −1 TOC ( Figure S5). For porous Ti/RuO 2 -TiO 2 @Pt and Ti/RuO 2 -IrO 2 @Pt, the kinetics constants reached the maximum value of 0.06 and 0.09 min −1 at a NaCl concentration of 3.5 g L −1 , respectively. The TOC removal reached 25.9% and 48.1% in 60 min of reaction for porous Ti/RuO 2 -TiO 2 @Pt and Ti/RuO 2 -IrO 2 @Pt, respectively ( Figure S5). The positive effect of the NaCl electrolyte was due to the oxidation of Cl −1 to active chlorine substances on the anode surface during the ECO process. Similar results were also reported in previous studies on the degradation of triclosan [46,47], rhodamine B [47,48], and enrofloxacin [47,49].

Effect of Current Density
In the ECO process, the current density applied in the system is a crucial parameter for the generation of hydroxyl radicals. An increase in the current density can accelerate the yield of •OH and enhance the electron transfer rate, but can also accelerate the oxygen evolution reaction and form a competing reaction with tetracycline degradation, which affects the electrode stability and increases the energy consumption [50,51]. Hence, the experiments for assessing the effect of current density on the tetracycline degradation efficiency were performed by applying current densities in the range of 10~40 mA cm −2 at an initial pH of 7 with 50 mg L −1 tetracycline and 3.5 g L −1 NaCl. As shown in Figure 4, by increasing the current density, the tetracycline degradation was dramatically enhanced; meanwhile, the amount of TOC removal was also increased. The porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrode exhibited the highest tetracycline degradation efficiency among the as-prepared electrodes. With the increase in current density, the reaction time of 100% tetracycline degradation was reduced from 15 min at 10 mA cm −2 to 5 min at 30 and 40 mA cm −2 , and the kinetic constant was increased from 0.23 to 1.29 min −1 . The kinetics of tetracycline degradation fitted well with the pseudo-first-order rate law with increasing current densities. Additionally, the TOC removal also increased from 25.4% to 39.8% as the current density increased from 10 to 40 mA cm −2 . When the current density increased from 10 to 20 mA cm −2 , the TOC removal ratio increased by 13.4% after a 20 min reaction time, and when further increasing the current density to 40 mA cm −2 , the amount of TOC removal increased slowly ( Figure S6). As a result, the best energy consumption (EC) for the porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrode was 167 kW kg −1 TOC at the current density of 20 mA cm −2 in the tetracycline degradation process. For the porous Ti/RuO 2 -IrO 2 @Pt and Ti/RuO 2 -TiO 2 @Pt electrode, the tetracycline degradation, kinetic constant, and TOC removal displayed a positive correlation with the current density, and the most efficient result was obtained by using the porous Ti/RuO 2 -IrO 2 @Pt electrode at 40 mA cm −2 for a reaction of 60 min. Molecules 2023, 28, x FOR PEER REVIEW 6 of 16  moval increased slowly ( Figure S6). As a result, the best energy consumption (EC) for the porous Ti/Y2O3-RuO2-TiO2@Pt electrode was 167 kW kg −1 TOC at the current density of 20 mA cm −2 in the tetracycline degradation process. For the porous Ti/RuO2-IrO2@Pt and Ti/RuO2-TiO2@Pt electrode, the tetracycline degradation, kinetic constant, and TOC removal displayed a positive correlation with the current density, and the most efficient result was obtained by using the porous Ti/RuO2-IrO2@Pt electrode at 40 mA cm −2 for a reaction of 60 min.

Effect of Initial Tetracycline Concentration and pH
For practical applications, the initial tetracycline concentration is an important factor that affects the ECO performance. In this work, initial concentrations in the range of 50-200 mg L −1 were examined in regard to the degradation of tetracycline. As shown in Figure 5, the removal efficiency decreased with the increase in the tetracycline concentration for all the electrodes. For the porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrode, removal rates of tetracycline ranging from 82.9% to 100% were achieved in a 20 min reaction time, which was much higher than that of the other two electrodes. We also observed that porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrodes exhibited good electrocatalytic performance at low tetracycline concentration, and the k value was reduced from 0.55 to 0.12 min −1 . This indicated that the electrocatalytic reaction was probably controlled by the surface adsorption and reaction process, rather than the mass transfer control. The initial pH value was taken into account to evaluate its effect on the electrocatalytic degradation of tetracycline ( Figure 6). For all the reaction systems with porous Ti/RuO 2 -TiO 2 @Pt, Ti/RuO 2 -IrO 2 @Pt, and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrodes, the initial pH showed a nonsignificant effect on the tetracycline degradation (more than 95% tetracycline removal efficiency), which suggested that the electrodes exhibited good applicability for tetracycline degradation in a wide pH range [52,53]. Commonly, the removal efficiency of tetracycline was faster in acidic conditions than in basic ones. This may be ascribed to the acceleration of •OH production under acidic conditions, and the •OH displayed higher oxidation capability in acidic pH (2.85 V) than in alkaline pH (2.02 V). In addition, for porous Ti/RuO 2 -IrO 2 @Pt and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrodes, the influence of the initial pH value was slightly higher than that observed for the porous Ti/RuO 2 -TiO 2 @Pt electrode. trodes exhibited good applicability for tetracycline degradation in a wide pH range [52,53]. Commonly, the removal efficiency of tetracycline was faster in acidic conditions than in basic ones. This may be ascribed to the acceleration of •OH production under acidic conditions, and the •OH displayed higher oxidation capability in acidic pH (2.85 V) than in alkaline pH (2.02 V). In addition, for porous Ti/RuO2-IrO2@Pt and Ti/Y2O3-RuO2-TiO2@Pt electrodes, the influence of the initial pH value was slightly higher than that observed for the porous Ti/RuO2-TiO2@Pt electrode.

Analysis of •OH Production
In the ECO process, •OH production was considered the main factor that triggers the degradation of tetracycline [54,55]. Therefore, it was important to monitor the •OH generation during the ECO treatment. Herein, terephthalic acid was used to capture the

Analysis of •OH Production
In the ECO process, •OH production was considered the main factor that triggers the degradation of tetracycline [54,55]. Therefore, it was important to monitor the •OH generation during the ECO treatment. Herein, terephthalic acid was used to capture the generated •OH to form a fluorescent byproduct, 2-hydroxy terephthalic acid. As shown in Figure 7, the fluorescence intensity was used to represent the amount of •OH. For all the electrodes, we observed that the fluorescence intensity around 425 nm increased along with the reaction time, which confirmed that •OH was continuously produced on the anode surface. Comparing the fluorescence intensity of all the electrodes indicated that the commercial Ti/RuO 2 -IrO 2 had the lowest fluorescence intensity among the electrodes, which was probably due to its planar structure and its lower ECSA. Therefore, the porous electrodes had a higher oxidation capability compared with the planar ones.  Figure 8 depicts the results of our evaluation of the degradation efficiency and energy consumption of tetracycline degradation displayed by the obtained anodes under the same reaction conditions. As shown in Figure 8a, the porous Ti/Y2O3-RuO2-TiO2@Pt electrode achieved 100% tetracycline degradation in 20 min corresponding to a k value of 0.55 min −1 , which was much faster than the other electrodes. Meanwhile, 38.2% TOC removal was also reached after a reaction of 20 min (Figure 8b). For planar Ti/RuO2-IrO2, with porous Ti/RuO2-TiO2@Pt electrodes, the TOC removal was only about 24.0% and 25.9% in 60 min, respectively. On the other hand, for porous Ti/RuO2-IrO2@Pt electrodes, 48.1% TOC removal was achieved in 60 min. Figure 8c shows the energy consumption comparison. The EC results can be expressed in the following order: porous Ti/RuO2-TiO2@Pt (738 kWh kg −1 TOC), planar Ti/RuO2-IrO2 (621 kWh kg −1 TOC), porous Ti/RuO2-IrO2@Pt (312 kWh kg −1 TOC), and porous Ti/Y2O3-RuO2-TiO2@Pt (167 kWh kg −1 TOC), when comparing all the tested anodes. Their continuous operation was further tested. As shown in Figure 8d, it was observed that all the porous electrodes displayed a stable performance for tetracycline degradation under continuous operation [56,57]. Based on the above-mentioned comparison, it can be concluded that the ECO technology with porous electrodes repre-  Figure 8 depicts the results of our evaluation of the degradation efficiency and energy consumption of tetracycline degradation displayed by the obtained anodes under the same reaction conditions. As shown in Figure 8a, the porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt electrode achieved 100% tetracycline degradation in 20 min corresponding to a k value of 0.55 min −1 , which was much faster than the other electrodes. Meanwhile, 38.2% TOC removal was also reached after a reaction of 20 min (Figure 8b). For planar Ti/RuO 2 -IrO 2 , with porous Ti/RuO 2 -TiO 2 @Pt electrodes, the TOC removal was only about 24.0% and 25.9% in 60 min, respectively. On the other hand, for porous Ti/RuO 2 -IrO 2 @Pt electrodes, 48.1% TOC removal was achieved in 60 min. Figure 8c shows the energy consumption comparison. The EC results can be expressed in the following order: porous Ti/RuO 2 -TiO 2 @Pt (738 kWh kg −1 TOC), planar Ti/RuO 2 -IrO 2 (621 kWh kg −1 TOC), porous Ti/RuO 2 -IrO 2 @Pt (312 kWh kg −1 TOC), and porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt (167 kWh kg −1 TOC), when comparing all the tested anodes. Their continuous operation was further tested. As shown in Figure 8d, it was observed that all the porous electrodes displayed a stable performance for tetracycline degradation under continuous operation [56,57]. Based on the above-mentioned comparison, it can be concluded that the ECO technology with porous electrodes represents an efficient alternative due to its low energy consumption and high oxidation efficiency.

Electrode Preparation
First, the porous titanium plates were ultrasonically cleaned with deionized water, acetone, and ethanol for 30 min to remove the surface oil. The three nanoparticle powders prepared by means of the microemulsion method ( Figure 9) were dissolved in C 3 H 8 O to form a stable and dispersed coating solution. Then, the porous titanium plate was impregnated in the coating solution at vacuum and calcined in the muffle furnace at 350 • C for 15 min. After repeated impregnation and calcination, which was conducted 25 times, porous Ti/RuO 2 -IrO 2 @Pt, porous Ti/RuO 2 -TiO 2 @Pt, and porous Ti/Y 2 O 3 -TiO 2 -RuO 2 @Pt electrodes were finally prepared via calcination at 450 • C for 2 h in a muffle furnace.

Electrode Characterization and Electrochemical Testing
The morphology of the electrodes was analyzed using a scanning electron microscope (SEM, Zeiss Gemini 300, Jena, Germany). We used an X-ray diffractometer (XRD) (D/max2200PC, Japan) with a Cu Kα ray (λ = 0.15406 nm), a scanning voltage of 20 kV, a scanning step of 0.015°, a scanning speed of 1 s/step, and a scanning range of 10°-90° for XRD analysis. Fluorescence spectroscopy (Edinburgh FS5, UK) was performed in the measurement range of 365-535 nm with an excitation wavelength set at 315 nm and an emission wavelength set at 425 nm. The porosity and pore size distribution of porous titanium-based electrodes were analyzed using a mercury piezometer (Micromeritics Au-toPore IV 9500, Norcross, GA, USA).
The electrochemical characterization of the composite electrodes was performed using an electrochemical workstation (CHI660E, Shanghai Chenhua Instruments Co., Ltd., Shanghai, China). A three-electrode system was used, with a saturated calomel electrode as the reference electrode, a platinum sheet electrode as the auxiliary electrode, and the prepared porous anodes as the working electrode. Furthermore, 1 mol L −1 KOH was used as the electrolyte, and the electrode was subjected to cyclic voltammetry (CV) testing and linear scanning voltammetry (LSV) testing. Finally, the stability of the electrode was evaluated by means of intensive lifetime testing under 1 mol L −1 H2SO4 as the electrolyte and a 2 A cm −2 current density.
The prepared porous titanium composite electrode was used as the anode and the titanium plate was used as the cathode, and a DC regulated power supply was connected

Electrode Characterization and Electrochemical Testing
The morphology of the electrodes was analyzed using a scanning electron microscope (SEM, Zeiss Gemini 300, Jena, Germany). We used an X-ray diffractometer (XRD) (D/max2200PC, Tokyo, Japan) with a Cu Kα ray (λ = 0.15406 nm), a scanning voltage of 20 kV, a scanning step of 0.015 • , a scanning speed of 1 s/step, and a scanning range of 10 • -90 • for XRD analysis. Fluorescence spectroscopy (Edinburgh FS5, Livingstone, UK) was performed in the measurement range of 365-535 nm with an excitation wavelength set at 315 nm and an emission wavelength set at 425 nm. The porosity and pore size distribution of porous titanium-based electrodes were analyzed using a mercury piezometer (Micromeritics AutoPore IV 9500, Norcross, GA, USA).
The electrochemical characterization of the composite electrodes was performed using an electrochemical workstation (CHI660E, Shanghai Chenhua Instruments Co., Ltd., Shanghai, China). A three-electrode system was used, with a saturated calomel electrode as the reference electrode, a platinum sheet electrode as the auxiliary electrode, and the prepared porous anodes as the working electrode. Furthermore, 1 mol L −1 KOH was used as the electrolyte, and the electrode was subjected to cyclic voltammetry (CV) testing and linear scanning voltammetry (LSV) testing. Finally, the stability of the electrode was evaluated by means of intensive lifetime testing under 1 mol L −1 H 2 SO 4 as the electrolyte and a 2 A cm −2 current density.
The prepared porous titanium composite electrode was used as the anode and the titanium plate was used as the cathode, and a DC regulated power supply was connected to the cathode and anode. For degradation, the distance between the two electrodes was fixed at 2 cm, the area of the electrode immersed in the wastewater was 3 cm 2 , and the degradation was carried out under magnetic stirring and other conditions for 1 h. The effects of different factors (electrolyte type and concentration, current density, initial concentration, pH) on the performance of the electrode degradation of tetracycline were investigated and the optimal conditions were derived. Under optimal conditions, continuous degradation experiments were carried out, with 20 consecutive degradations for a total of 20 h, and samples were taken every hour.
Tetracycline degradation conformed to the pseudo-first-order kinetic model [58], and was calculated by means of Equation (1): where C 0 and C t are the initial concentrations of the pollutant (mg L −1 ) and the concentration with reaction time t (mg L −1 ); K is the pseudo-first-order kinetic rate constant (min −1 ).
The changes in TOC during the reaction were analyzed using a total organic carbon analyzer with the NPOC method. The energy consumption of the metal composite electrode in the electrochemical oxidation and degradation of tetracycline is expressed as kWh kg −1 TOC; that is, the electrical energy consumed for each removal of 1 kg TOC [59,60], calculated using Equation (2): where U is the voltage (V), I is the current (A), t is the reaction time (h), V is the volume of solution (L), and ∆TOC is the amount of TOC removed from the solution at time t (mg L −1 ).

Conclusions
In this work, porous anodes (Ti/RuO 2 -TiO 2 @Pt, Ti/RuO 2 -IrO 2 @Pt, and Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt) were fabricated with a high porosity titanium plate as the substrates. Compared with the planar anode, porous anodes exhibited a larger electrochemical active surface area and a longer service life. The indirect oxidation process triggered by •OH was proven to be responsible for the efficient tetracycline degradation. The porous Ti/Y 2 O 3 -RuO 2 -TiO 2 @Pt anode was found to have the fastest degradation rate of tetracycline and lower energy consumption compared with other anodes with different compositions, which was ascribed to its excellent electrochemical properties. This study thus presents alternatives for the practical application of ECO technology, providing a new option in the form of porous, highly efficient, and long serving life anodes for future industrial application.