Cobalt-Doped Black TiO2 Nanotube Array as a Stable Anode for Oxygen Evolution and Electrochemical Wastewater Treatment

TiO2 has long been recognized as a stable and reusable photocatalyst for water splitting and pollution control. However, it is an inefficient anode material in the absence of photoactivation due to its low electron conductivity. To overcome this limitation, a series of conductive TiO2 nanotube array electrodes have been developed. Even though nanotube arrays are effective for electrochemical oxidation initially, deactivation is often observed within a few hours. To overcome the problem of deactivation, we have synthesized cobalt-doped Black-TiO2 nanotube array (Co-Black NTA) electrodes that are stable for more than 200 h of continuous operation in a NaClO4 electrolyte at 10 mA cm–2. Using X-ray photoelectron spectroscopy, X-ray absorption spectroscopy, electron paramagnetic resonance spectroscopy, and DFT simulations, we are able to show that bulk oxygen vacancies (Ov) are the primary source of the enhanced conductivity of Co-Black. Cobalt doping both creates and stabilizes surficial oxygen vacancies, Ov, and thus prevents surface passivation. The Co-Black electrodes outperform dimensionally stable IrO2 anodes (DSA) in the electrolytic oxidation of organic-rich wastewater. Increasing the loading of Co leads to the formation of a CoOx film on top of Co-Black electrode. The CoOx/Co-Black composite electrode was found to have a lower OER overpotential (352 mV) in comparison to a DSA IrO2 (434 mV) electrode and a stability that is greater than 200 h in a 1.0 M KOH electrolyte at a current density of 10 mA cm–2.


■ INTRODUCTION
TiO 2 has long been recognized as a stable and reusable photocatalyst for water splitting and pollution. 1 However, potential applications of TiO 2 are most often correlated with its oxygen evolution reaction (OER) potential. 1,2 In spite of success in laboratory-scale research, many challenges remain with respect to the use of TiO 2 in solar fuel production and environmental remediation due to (1) its high band-gap energy of 3.2 eV (i.e., 385 nm) and (2) high attenuation coefficients for the penetration of incident UV photons in turbid water (i.e., both freshwater and wastewater). Some of these intrinsic barriers can be overcome when TiO 2 is used in electrochemical systems applications without the need for direct photoactivation of TiO 2 . 3,4 However, the low mobile carrier conductivity of n-type TiO 2 impedes its use as an electrocatalyst. The transport of electrons across the electrolyte/TiO 2 interface requires a large anodic potential (>3 V Ag/AgCl ) to overcome a high Schottky barrier. 4 The electronic properties of TiO 2 can be tuned by selfdoping. It is known that H 2 reduction could introduce Ti 3+ , oxygen vacancies, and surface disorders to TiO 2 . The resultant Black TiO 2 has a narrower band gap. 5−7 Black TiO 2 catalysts on both anatase and rutile structures exhibited high activity in visible-light-driven water oxidation. 8,9 However, their activity during dark electrolysis has been less explored. Reducing TiO 2 in pure H 2 at temperatures over 1000°C promotes the bulk phase transition from anatase to substoichiometric Magneĺi phase Ti 4 O 7 . 10 Magneĺi phase TiO 2 has conductivities that approach 11 orders of magnitude greater than that of TiO 2 . 11 Thus, it has been shown to be a stable anode material for water oxidation and wastewater treatment. 12,13 Given that the preparation of Ti 4 O 7 requires highly reducing conditions, it is often difficult to prepare conductive, stoichiometric TiO 2 using conventional techniques. Recently, conductive TiO 2 nanotube arrays (NTAs) that are either blue or black in appearance have been reported. Black NTAs were prepared by reducing anatase NTA under an H 2 or H 2 /Ar atmosphere at 450−550°C. 14,15 Blue NTAs were obtained by cathodization of anatase NTA in aqueous electrolyte. 16−20 Conductive NTA electrodes have satisfactory electrochemical oxidation activity. 20,21 The synthetic preparation procedures for Blue and Black NTA are less stringent than those of the Magneĺi phases, Ti x O 2x−1 .
Conductive NTAs supported on titanium plates have a major advantage over particulate electrocatalysts, since they can be utilized directly as electrodes without the need for additional adhesive substrates or organic binders. However, deactivation of both Blue and Black NTAs has been observed after a few hours of electrocatalysis due to the surface passivation. 20,21 Therefore, electrodes made from these materials are currently impractical for engineering applications.
In this study, we report on the effect of doping trace amounts of cobalt onto Black TiO 2 NTA (Co-Black NTA) that results in a lowering of the OER overpotential and increases electrode stability. Even though bulk CoO x is reported to be unstable for the OER at pH <12 in phosphate-free electrolyte solutions, 22,23 we observe that CoO x is immobilized and stable on Black NTAs even at circumneutral pH. We show that Co-Black electrodes outperform an IrO 2 -based dimensionally stable anode (DSA) for oxidative electrochemical wastewater treatment. We also found that the increase of Co loading forms a CoO x film on top of Co-Black substrate. The resultant CoO x / Co-Black composite electrode exhibits high OER activity (overpotential of 352 mV vs 434 mV for IrO 2 DSA) and stability (>200 h) in 1 M KOH electrolyte at 10 mA cm −2 .

■ EXPERIMENTAL SECTION
Electrode Preparation. The overall approach to synthesize NTA electrodes is schematically illustrated in Figure 1a. Amorphous TiO 2 NTA (Am-NTA) was prepared by anodization of a Ti plate (6 cm 2 , 0.5 mm) at 42 V in ethylene glycol (EG) electrolyte with 0.25 wt % NH 4 F and 2 wt % H 2 O for 6 h. 24 After anodization, Am-NTA was subjected to a second anodization in 5 wt % H 3 PO 4 /EG electrolyte at 42 V for 1 h to enhance its mechanical stability. 20,25 Cobalt-loaded Am-NTA (Co/Am-NTA) was prepared by dipping Am-NTA into 250 mM Co(NO 3 ) 2 /ethanol solution. The sample was dipped into the coating solution for 1 min, pulled up at the rate of 10 mm/min, and finally dried at room temperature for 2 min. The dip-coating processes were repeated three times. The Co loading was determined by ICP-MS (Agilent 8800) as 0.54 ± 0.12 μmol/cm 2 . Lowering the Co(NO 3 ) 2 concentration in the dip-coating solutions to 50 and 25 mM produced Co(0.25)-and Co(0.17)-Black NTA with Co loadings of 0.25 and 0.17 μmol/cm 2 , respectively.
Annealing Am-NTA and Co/Am-NTA in air at 450°C for 1 h yieldeds NTA and Co-NTA, respectively. Black NTA and Co-doped Black NTA (Co-Black) were obtained by annealing Am-NTA and Co/Am-NTA in a stream of 5% H 2 /Ar at 450°C for 30 min and then naturally cooling to room temperature. The Blue NTA was prepared by applying a cathodic current of 5 mA cm −2 on the NTA electrode for 10 min in 0.1 M potassium phosphate buffer solution (KPi). All of the thermally treated NTAs were determined to be in the anatase phase by XRD ( Figure S1). Five control samples were prepared. (1) A cobalt-doped TiO 2 (Co-TiO 2 ) film electrode was prepared by spray-coating a mixture of 250 mM titanium−glycolate complex and 25 mM Co(NO 3 ) 2 onto a Ti plate, followed by annealing in air at 450°C for 1 h. 26 The final mass loading of Co-TiO 2 was 6 mg/cm 2 . The molar Co loading was 0.6 μmol/cm 2 . (2) Amorphous cobalt hydroxide was loaded onto a Ti plate (Co(OH) x /Ti) by the electrochemical deposition method described previously, 27 with the modification of replacing the glassy-carbon substrate with a titanium plate. (3) Cobalt oxide was coated onto the Ti plate (CoO x /Ti) by a drop-casting method using 250 mM Co(NO 3 ) in ethanol as precursor,
Catalyst Characterization. Cyclic voltammetry (CV) and electrochemical impedance spectroscopy (EIS) were measured using a Biologic VSP-300 potentiostat. Uncompensated resistance (R u ) was measured by EIS. All of the presented anodic potentials were corrected by R u . EIS was also used to determine Mott−Schottky plots. These details are described in Text S2 of the Supporting Information. For two-point solidstate measurements, nanotube tops were contacted by sputterevaporated 10 nm thick Au using a Cressington 208HR sputter coater. Then resistance was obtained from the I−V curves collected by potentiostat.
After CV analyses, NTA electrodes were characterized by scanning electron microscopy (SEM, ZEISS 1550VP) coupled with energy dispersive X-ray spectroscopy (EDS), scanning transmission electron microscopy (STEM, FEI TF30ST) equipped with a high angle annular dark field (HAADF) detector, X-ray photoelectron spectroscopy (XPS) with Surface Science M-Probe ESCA/XPS, and X-ray diffractometry (PANalytical X'Pert Pro). Electron paramagnetic resonance spectra were collected on a Bruker EMX X-band CW-EPR spectrometer at room temperature and 10 K. Powder samples were collected by scraping NTA from the Ti metal substrate.
X-ray Absorption Spectroscopy. X-ray absorption spectroscopy (XAS) of Ti L-edge and O K-edge were measured on Beamline 8.0.1 at the Advanced Light Source (ALS), Lawrence Berkeley National Laboratory. The resolutions of the measurements were 0.4 eV at the O K-edge and 0.3 eV at the Ti L-edge. Spectra were recorded in total electron yield mode (TEY) and were obtained by measurement of the sample drain photocurrent under irradiation with monochromatic light. The XAS at Co K-edge was conducted at BL17C1 at the National Synchrotron Radiation Research Center, Taiwan. The photon energy calibrations of the XAS spectra at the Ti L-edge and O K-edge were conducted on the basis of the reference anatase TiO 2 films. The incident radiation flux was monitored by the photocurrent produced in a gold mesh in the beam path. All spectra were normalized to the incident flux recorded with Au mesh.
Cobalt Leaching and Anodic Stability Testing. The Co-Black NTA electrodes were subjected to cathodization (−5 mA/cm 2 , 10 min), CV (−0.5 to +3 V RHE , 10 mV s −1 ), and four continuous stages of constant current electrolysis (10 mA cm −2 ) at an interval of 3 h. At the end of each step, a water sample was collected, acidified by HNO 3 , and then analyzed by ICP-MS (Agilent 8800) to determine the Co concentration. The electrolyte was replaced before the next test. The anodic stability test was performed following the constant current Co leaching test. Current density was maintained at 10 mA cm −2 . Electrolyte was replaced every 12 h.
OER, CER, and Water Treatment Tests. OER activities were evaluated using Tafel plots, which were collected by potentiostat with a three-electrode configuration. Stainless steel and saturated Ag/AgCl were used as counter and reference electrodes, respectively. Data were collected at constant current mode (0.01−10 mA cm −2 ). Each current step was maintained for 5 min to measure the steady-state anodic potential.
Hydroxyl radical production and direct electron transfer activities were measured using benzoic acid and oxalate as probe molecules, respectively. Benzoic acid was measured by HPLC (Agilent 1100) equipped with a Zorbax XDB column. Oxalate was analyzed by ion chromatography (ICS 2000, Dionex). Free chlorine concentrations ([FC]) were measured using the DPD (N,N-diethyl-p-phenylenediamine) reagent (Hach method 10102). The current efficiency was estimated using the equation

ACS Catalysis
where V is electrolyte volume (25 mL), F is the Faraday constant (96485 C mol −1 ), and I is the current (A). Chemical oxygen demand (COD) in wastewater was determined by the dichromate digestion method (Hach Method 8000). NH 4 + was quantified by ion chromatography.
Latrine wastewater was collected from a recycling electrochemical toilet system located on the Caltech campus (Pasadena, CA). The latrine wastewater has a pH of around 8.5 with a conductivity of 13.5 mS cm −1 . It contains 500 mg L −1 COD and 18.5 mM NH 4 + . During the electrolysis of latrine wastewater, the Co-Black and IrO 2 electrodes were operated at 10 mA cm −2 with cell voltages of 4.6 and 4 V, respectively. The electrode area/wastewater volume ratio was set as 60 m −1 .

■ RESULTS AND DISCUSSION
The electrochemical activity of electrodes was determined by cyclic voltammetry (CV) in potassium dihydrogen phosphate (KPi) buffer solutions. The anodic branch current response is due to the OER. Both NTA and Co-NTA have low OER activity, as indicated by the low current densities of Figure 1b. The Co-TiO 2 film electrode has higher current response in comparison to NTA and Co-NTA, but its performance is inferior to that of conductive NTA electrodes (Figure 1b vs Figure 1c). An increase in current response is observed on both the Blue and Black NTA electrodes at onset potentials of 2.7 and 1.7 V, respectively (Figure 1c). Co-Black NTA has the highest OER activity due to its lower onset potential and its higher current density. There have been previous reports that Co-doped TiO 2 nanotubes could be used as photoelectrochemical water-splitting catalysts. 28−31 However, their photocurrent densities are less than 5 mA/cm 2 . In a recent report, Co 3 O 4 / TiO 2 nanotubes were used for dark water electrolysis. 32 However, it appeared that TiO 2 functioned only as an inert substrate for Co 3 O 4 with resulting current densities <1 mA/cm 2 at an applied potential of 2.3 V RHE . These results are in agreement with the inert performance observed on a Co-TiO 2 film electrode with 0.6 μmol/cm 2 Co loading prepared in this study. In contrast, Co-Black NTA with less Co loading (0.54 μmol/cm 2 ) exhibits 200 times higher current density in comparison with a Co-TiO 2 film electrode at 2.3 V RHE . This finding highlights the promotional role of conductive NTA substrate on the OER activity of Co-TiO 2 system.
The anodic stability of the NTA electrodes at circumneutral pH was determined by applying a constant current of 10 mA cm −2 in a KClO 4 electrolyte solution. Deactivation of the electrode was determined from the sharp increase in anodic potential ( Figure 2a). The Blue and Black NTAs have lifetimes of 2.3 and 4 h, respectively, which are in line with previous studies. 20,21 A substantially longer lifetime and apparent stability (>200 h) were observed for the Co-Black NTA electrode (Figure 2b). Lowering the Co loading to 0.25 and 0.17 μmol/cm 2 does not affect the stability of Co-Black NTA within the investigated 100 h electrolysis ( Figure S2a). The results suggest that a trace amount of the Co dopant is sufficient to significantly enhance the stability of Black NTA. Figure 2c shows that the Co-Black electrode is also stable in 1.0 M KOH. However, deactivation occurs after 45 h in 0.5 M H 2 SO 4 . Nevertheless, Co-Black electrode still has a longer lifetime than Black NTA (insert of Figure 2c). We further investigated the leaching of Co in different electrolytes at cathodic (−5 mA cm −2 ), fluctuating (CV), and anodic (10 mA cm −2 ) currents ( Figure 2d). Complete dissolution of Co from Co-Black was observed after sequential cathodization, CV, and 12 h electrolysis in H 2 SO 4 . In contrast, only 2.1% of Co was lost under similar conditions in the KOH electrolyte. Retarded Co leaching is also observed in the 0.1 M KPi electrolyte; this is probably due to the formation of less soluble CoPi. 33,34 In addition, the leaching of Co from Co-Black is undetectable (<0.03%) by ICP-MS after 9 h of electrolysis in KClO 4 in the absence of phosphate. Analyses by SEM-EDS and STEM-HAADF indicate that Co is well dispersed in Co-rich spots on

Research Article
Co-Black throughout the tube length. CoO x particles were not found ( Figures S3−S6).
Two-point solid-state conductivity measurements show that the resistances of Blue, Black, and Co-Black NTA electrodes are 5 orders of magnitude lower than that of pristine NTA electrodes ( Figure S7). Knowing that the above measurements may be interfered by the contact resistance of Au coating, we further probed the semimetallic properties of conductive NTA by EIS using liquid electrolyte contacts ( Figure S8). The Blue, Black, and Co-Black NTA all have good conductivity, but their OER activities vary. This implies that, in addition to bulk conductivity considerations, surface specific characteristics need to be considered.
Both electrochemical and thermal reduction should promote the formation of Ti 3+ sites and adjacent oxygen vacancies (O v s) on TiO 2 . However, aside from Ti 4+ , X-ray photoelectron spectroscopy (XPS) cannot confirm the existence of Ti 3+ on Blue and Black NTA, probably due to the reoxidation of Ti 3+ to Ti 4+ in ambient air ( Figure S9). Nevertheless, the oxidation of Ti 3+ is essentially the filling of O v by adsorbed oxygen species, which can be detected by XPS ( Figure S10). The relative concentration of absorbed oxygen species is associated with the abundance of nascent O v . The XPS O 1s spectrum reveals that the concentration of oxygen vacancies (O v ) decreases in the order Black (22%) > Blue (17%) > pristine NTA (12%). XPS analyses also found that Co doping results in a significant reduction in the Ti oxidation state in Co-Black NTA and creates more surficial O v (25%) (Figures S9 and S10).
The NTA samples were further investigated using X-ray absorption spectroscopy (XAS) operated in total electron yield (TEY) mode. The results obtained from TEY mode involved both surface and subsurface characteristics, as XAS has a larger sampling depth in comparison to XPS. The Ti L-edge XAS is shown in Figure 3a. The spectra that result from the transition of electrons from the Ti 2p 3/2 and 2p 1/2 initial states to the unoccupied 3d orbital. Peaks A−C correspond to the electronic transition from 2p 3/2 to 3d, while peaks D and E can be assigned to the transition from 2p 1/2 to 3d. 35 The single crystal of TiO 2 has octahedral (O h ) symmetry. The O h crystal field splits the Ti 3d band into t 2g and e g degenerate orbitals. The excitation of electrons from the ground state of Ti 4+ to t 2g orbital can be expressed as 2p 6 3d 0 → 2p 5 3d 1 , which is reflected as the energy absorption at 458 eV (peak A). Ti 3+ (2p 6 3d 1 ) already has one electron in the t 2g orbital, which reduces the number of unoccupied states. Therefore, the presence of Ti 3+ leads to the reduction of t 2g relative intensity and e g peak width broadening. 35 The lesser resolved peaks B and C, the reduction of the A/B intensity ratio (Figure 3c), and the shift of peak A to lower energy confirm the presence of Ti 3+ in Blue and Black NTA as well. 35,36 The O K-edge XAS is shown in Figure 3b. Peaks a and b can be assigned to the electronic transition from O 1s to O 2p hybridized with the Ti 3d t 2g and 3d e g states, respectively. 37,38 The peak intensity ratio of t 2g to e g is lower in Blue and Black NTA (Figure 3c), which suggests the presence of more Ti 3+ and O v . 35 In agreement with the XPS analyses, Co-Black has the highest number of Ti 3+ and O v , sites as supported by the lowest peak A/B and a/b ratios in XAS (Figure 3c).
We further investigated the oxidation state and coordination environment of Co dopant by XAS. The absorption edge in Co K-edge XAS spectra of Co-Black overlaps with that of CoO ( Figure 3d); this implies that surficial Co ions of Co-Black are in valence 2+, which is in line with the XPS analyses ( Figure   S9), and the EPR results (vide infra). The pre-edge peaks of CoO and Co 3 O 4 correspond to the 1s−3d electronic transitions contributed by the tetrahedrally coordinated Co 2+ . This feature is less pronounced for Co-Black, indicating that Co 2+ is in an O h configuration in which 1s−3d electronic transitions rarely occur. 39 The overall Co K-edge profile of Co-Black is different from that of CoO and Co 3 O 4 . This results again suggest that the coordination structure of Co 2+ ions in Co-Black is clearly different from that of oxide particles. Given that no CoO x particulates could be found by both SEM and TEM, it is possible that Co 2+ is atomically doped into the lattice of TiO 2 , adopting the same O h configuration. This assumption needs to be verified by aberration-corrected TEM in a future study.
The coordination structure of Co 2+ remains intact after 100 h of electrolysis, as indicated by the unchanged Co K-edge profiles of Co-Black before and after use (Figure 3d). Of note, XPS data indicated that Co 2+ in Co-NTA was prepared by annealing the Co(NO 3 ) 2 loaded Am-NTA in air, even though the calcination of Co(NO 3 ) 2 alone produced Co 3 O 4 (i.e., a mixed Co(III)/Co(II) material). ( Figure S9). These observations combined suggest that Co 2+ is effectively immobilized on NTA and its reduced valence state does not result from H 2 reduction but from a strong Co−TiO 2 interaction. It is noteworthy that Co 2+ in CoO x is a labile OER intermediate that tends to be dissolved at neutral pH in the absence of phosphate. 23,33 Our findings suggest that the Co−TiO 2 interaction is strong enough to prevent Co leaching at circumneutral pH. These results could provide a new strategy to prepare stable CoO x -based OER catalysts.
NTA samples were scraped off from Ti substrate for EPR characterization. The EPR signals of powdered NTA samples should mainly reflect their bulk characteristics. Signals were normalized by sample weight in order to perform semiquantitative comparison. The EPR signal at a g value of 2.003 could be attributed to electrons localized on O v . 14,40 As shown above, XPS and XAS unambiguously point out that Blue NTA has more surficial O v than pristine NTA. However, higher bulk phase O v concentration is not observed on Blue NTA, as shown by EPR (Figure 4a), implying that electrochemical reduction only results in changes on the surface/subsurface of Blue NTA. The results seem to be reasonable, since the mild electrochemical reduction that was carried out at room temperature is less likely to dislodge bulk lattice oxygen. In contrast, H 2assisted thermal reduction largely increases the bulk O v concentration of Black NTA, which is reflected as an 80 times increase in peak intensity in the EPR spectrum ( Figure  4b).
In comparison with Black NTA, Co-Black has an O v signal with lower intensity (Figure 4b). However, such a discrepancy is eliminated in EPR spectra recorded at 10 K (Figure 4c). In addition, Co-Black shows an EPR signal at g = 4.2, which could be assigned to high-spin (S = 3/2) Co 2+ in an O h environment. 41 The results combined imply (1) the bulk O v concentration of Co-Black NTA is commensurate with that of Black NTA and (2) the Co 2+ centers enhance relaxation of unpaired electrons of neighboring O v sites. As a consequence, the O v resonance signal of Co-Black is attenuated at room temperature. As shown in the inset of Figure 4c, resonance signals at g = 1.92, which can be attributed to Ti 3+ , 42 were observed on both Black and Co-Black NTA. The Co-Black NTA has more Ti 3+ sites, resulting in a higher signal intensity.
The Ti 3+ −O v pairs serve as electron donors to facilitate bulk conductivity. Thus, the elevated conductivity of Black NTA and

Research Article
Co-Black NTA in comparison with pristine NTA can be assigned to the increase in bulk O v concentration (Figure 4d). For the Blue NTA, the mechanism seems to be more complicated. It is suspected that electrochemical reduction only makes the surface/subsurface of Blue NTA conductive. Thanks to its vertically aligned tubular structure, electrons are able to transfer to the Ti substrate through the "conductive skin" of Blue NTA. In contrast, as we proved previously, the TiO 2 film electrode without such a structure cannot gain anodic conductivity after electrochemical reduction, 20 probably due to the presence of underlying, insulating bulk TiO 2 .
Good conductivity is a prerequisite for electrocatalysts, while their catalytic activity is determined by the number of active sites. The surficial O v is generally considered as an active site for the OER. 43,44 It exposes unsaturated metal ions, which in turn lead to the adsorption and dissociation of H 2 O. 45,46 Black NTA has more surficial O v sites and thus has a lower onset potential for the OER and a correspondingly higher activity in comparison to the Blue NTA. Clearly, the highest observed OER activity of Co-Black NTA electrodes can be attributed to the higher abundance of O v . The pristine NTA also has surficial O v , but the lack of bulk O v impedes bulk phase electron transport. As a consequence, pristine NTA has no discernible OER activity. The same rule can be invoked to explain the inert OER activity of Co-NTA and Co-TiO 2 film electrode ( Figure  1b).
Computational simulation using density functional theory (DFT) was performed to provide insight into the mechanism of Co−TiO 2 interactions at an atomic level (detail can be found in Text S1). Simulations were focused on the TiO 2 (101) plane because (1) as observed by HRTEM (Figure S5a), the tube wall is mainly composed of (101) plane, which in line with the observation of a previous study, 47 and (2) XRD analyses show that the (101) plane is sensitive to surface fabrication, as the Co doping only affects the crystallinity of the (101) plane, while other planes remain intact ( Figure S1). The DFT simulation found that O v formation is more favorable by 3.6 eV when the neighboring Ti is substituted by Co ( Figure 5). This is because . 48 The simulation also shows that the O atoms which are not directly bonded to Co tend to form vacancies as well, indicating a nonlocal effect. Since the formation of O v reduces the coordination of the metal ions, the apparent oxidation states should be lower than those sites in the pristine material. This interpretation is in line with the reduced Ti and Co valence states in Co-Black.
The results of the DFT simulation imply that Co doping could thermodynamically stabilize surficial O v . This mechanism has a significant effect on electrode lifetime. For both Blue and Black NTA, deactivation could be ascribed to surface passivation due to the irreversible uptake of oxygen and subsequent loss of O v during prolonged OER. As shown in Figure 6, a reduction in the O v concentration from 22% to 16% was found on Black NTA after deactivation, while such a change could not be observed on Co-Black. The hypothesis presented above may explain the superior stability of Co-Black in comparison to Black NTA in H 2 SO 4 electrolyte solutions (insert of Figure 2c). The leaching of Co from Co-Black under acidic conditions may create additional O v s, which in turn enables Co-Black to have a longer lifetime than Black NTA. However, the newly formed O v s will not be stabilized by Co due to its loss via leaching from the Co-Black NTA matrix. Therefore, the deactivation will take place over time under acidic conditions. Two OER catalysts, nickel oxides and iron oxides, were loaded on Black NTA electrodes by dip coating. It is found that Ni-Black and Fe-Black NTA electrodes exhibit improved stability in comparison with Black NTA but they still suffered from deactivation after 40 h of electrolysis in KClO 4 electrolyte ( Figure S2a). No residual Ni and Fe could be detected on the deactivated electrodes, indicating the complete dissolution of NiO x and FeO x , which may be the cause of deactivation. From

ACS Catalysis
Research Article a thermodynamic point of view, the Pourbaix diagrams ( Figure  S2b) also indicate that NiO x and FeO x are more vulnerable to corrosion than CoO x under the conditions of a stability test (2.4−2.7 V RHE , pH 7). These results again highlight the importance of a strong Co−TiO 2 interaction on maintaining the anodic stability of Co-Black NTA electrode.
Two electrochemical applications, the OER and wastewater electrolysis, were tested using the Co-Black electrode. A IrO 2 DSA and a C-DSA with the same geometric surface area were chosen as reference benchmarks, since the DSA-IrO 2 electrode is generally recognized as an inherent standard for both OER and wastewater treatment. Tafel plots (Figure 7 and Figure  S11) indicate that Co-Black is less OER active than IrO 2 DSA at both neutral and alkaline pH.
It is found that the OER activity of Co-Black can be enhanced by increasing the Co loading. A Co(NO 3 ) 2 /ethanol solution was drop-casted onto a Co-Black electrode. The sample was then reduced in 5% H 2 /Ar at 450°C for 30 min. During annealing, a discrete film layer of amorphous CoO x formed on top of Co-Black ( Figures S12 and S13). The XPS analyses ( Figure S14) indicate that the Co of the CoO x film has higher valence (3+/2+) than that of Co-Black (2+) due to the absence of a Co−TiO 2 interaction. The Co*-Black composite electrode with a Co loading of 2.1 μmol cm −2 has over-potentials of 360 and 434 mV, respectively, at 1.0 and 10 mA cm −2 in 1 M KOH (Figure 7b). Increasing the Co loading to 4.2 μmol cm −2 gave a Co**-Black electrode with an even higher OER activity; this electrode has overpotentials of 289 and 352 mV at 1.0 and 10 mA cm −2 , respectively ( Figure 7b). The performance of Co**-Black is not only higher than those of IrO 2 DSA, C-DSA, and Co(OH) x /Ti but also superior to the reported activities of a benchmarking Co(OH) x /GC (400 mV at 10 mA cm −2 ), 27 Co 3 O 4 nanowires (320 mV at 1 mA cm −2 ), 49 Co 3 O 4 nanosheets (390 mV at 10 mA cm −2 ), 46 and Co@Co 3 O 4 nanoparticles (420 mV at 10 mA cm −2 ). 50 A detailed comparison of alkaline OER performance and catalyst parameters is provided in Table S1. The composition of the CoO x film was not optimized for the OER in this study. It is reasonable to believe that a higher OER activity could be achieved by doping Ni and Fe into the CoO x film. 51,52 The higher OER activity of Co**-Black electrode could be attributed to two primary factors. First, more OER active sites are created by the CoO x film. This effect is illustrated in Figure  S15, which shows that the double-layer capacitance, which is proportional to the electrochemically active surface area (ECSA), increases in the order Co-Black (7.5) < Co*-Black (12.4) < Co**-Black (21.4 mF cm −2 ). Co**-Black with 6 cm 2 geometric area has a large ECSA of 3210 cm 2 , giving a  . Tafel plots in different electrolytes. Co*-and Co**-Black were prepared by drop-casting 250 mM Co(NO 3 ) 2 /ethanol precursor on Co-Black, followed by annealing in 5% H 2 /Ar at 450°C for 30 min. CoO x /Ti was prepared by the same procedure except that a Ti plate was used as the supporting substrate. The Co loading was 2.1 μmol cm −2 for Co*-Black and 4.2 μmol cm −2 for Co**-Black and CoO x /Ti.

ACS Catalysis
Research Article roughness factor of 535 (Table S1). As shown in Figure S14, XPS analyses prove that Co**-Black has a higher O v concentration (32%) than Co-Black (25%  Figure S7), the CoO x /Ti composite electrode was found to has a lower OER activity in comparison to the Co**-Black electrode ( Figure 7b). As illustrated in Figure S16, Co**-Black is stable for more than 200 h in 1.0 M KOH at 10 mA cm −2 . In contrast, a gradual deactivation is observed for CoO x /Ti. Overall, these results indicate that the presence of Co-Black NTA as an interlayer prevents the passivation of the catalyst/Ti interface, which is a major challenge affecting the stability of DSA electrodes. 53 Although the Co-Black electrode is relatively inert with respect to the OER in comparison to a conventional IrO 2 DSA, it is found to be more active for the electrochemical production of reactive oxygen species and other oxidants (i.e., reactive chlorine species). Electrolysis of a 30 mM NaCl solution shows that Co-Black has a higher chlorine evolution rate (CER) than IrO 2 DSA ( Figure S17a). Using benzoic acid and oxalate ion as probe molecules, we show that Co-Black outperforms an IrO 2 DSA in terms of hydroxyl radical ( • OH) generation and direct electron transfer oxidation ( Figure S17b,c).
Co-Black was further applied for the treatment of latrine wastewater that was collected on the Caltech campus in a prototype solar toilet system. 26,54 Chloride (40 mM) that originated from human waste (i.e., urine) is oxidized to chlorine (e.g., HOCl, ClO − ). Hypochlorous acid, HOCl, reacts with ammonia (NH 3 /NH 4 + ) to form chloramines (e.g., NH 2 Cl, NHCl 2 ), which in turn undergo a self-reaction leading to denitrification with the offgassing of N 2 leading eventually to breakpoint chlorination. 26,54 Co-Black outperforms the IrO 2 DSA due to its higher CER activity (Figure 8a). Although C-DSA has a higher CER ( Figure S17), it still exhibits inferior NH 4 + removal performance in comparison to Co-Black. This is probably because Co-Black is more active for the removal of organics, which compete with NH 4 + to react with chlorine. Both chlorine and • OH contribute to the removal of organic pollutants (indexed in terms of chemical oxygen demand, COD). As expected, the COD removal capability of Co-Black is superior to that of IrO 2 DSA and C-DSA (Figure 8b). The effluent after 8 h of treatment is clear in appearance and suitable for nonpotable water reuse (Figure 8c).

■ CONCLUSIONS
In conclusion, the results of this study show that Co doping significantly extends the lifetime of Black NTA electrodes via tuning of the concentration and stability of oxygen vacancies, O v . Co-Black electrodes are shown to be effective in terms of electrochemical oxidation. Co-Black electrodes also function as the conductive substrates for CoO x -based OER catalysts. The simplicity of the synthetic procedures suggests that conductive TiO 2 NTA could be utilized for energy storage and industrial applications on a wider scale, provided that the operational lifetimes can be extended further.