As shown in
Fig. 3a, the benchmarked RuO
2 required 244 mV overpotential to obtain 10 mA/cm
2, outperforming the RuO
2-300 needing 266 mV overpotential to attain 10 mA/cm
2. Impressively, RuO
2/MnO
2 exhibited a robust catalytic activity towards acidic OER demanding 221 mV overpotential to obtain 10 mA/cm
2. The OER performance of RuO
2/MnO
2 was superior to RuO
2-300 attributing to the formation of heterostructure inducing more active sites as well as electronic configurations since MnO
2 exhibited an ignorable OER activity. Due to the different dosage of noble metal Ru, the mass activity (MA) was estimated shown in Fig. S5 (Supporting information). RuO
2/MnO
2 exhibited a 6.5-time higher mass activity by comparison with RuO
2-300 at 1.52 V
vs. RHE. Besides, the MA value of RuO
2/MnO
2 at 1.52 V
vs. RHE was boosted by a factor of 3.7 with relative to commercial RuO
2. As listed in Table S2 (Supporting information), it was noticed that RuO
2/MnO
2 exhibited a higher OER performance than reported Ru based electrocatalysts. The Tafel slope was 118.2 mV/dec, 91.1 mV/dec and 80.8 mV/dec for commercial RuO
2, RuO
2-300 and RuO
2/MnO
2 (
Fig. 3b). The lower Tafel slope of RuO
2/MnO
2 also indicated a Eley-Rideal-like (ER-like) OER mechanism; however, OER occurred on commercial IrO
2 followed Langmuir-Hinshelwood mechanism. Also, as displayed in Fig. S6 (Supporting information), the charge transfer resistance (
Rct) of RuO
2/MnO
2 was as low as 61.4 Ω, which was decreased by 28.8% and 31.4% than RuO
2-300 and commercial RuO
2. To know the activation energy for various electrocatalysts, OER performance tested at different temperatures were carried out (Fig. S7 in Supporting information). The activation energy was estimated as 35.04 kJ/mol and 19.17 kJ/mol for RuO
2-300 and RuO
2/MnO
2 shown in
Fig. 3c, respectively. The activation energy for acidic OER catalysis was strongly decreased by 45.7% for RuO
2/MnO
2 with respect to RuO
2-300 suggesting its better catalytic activity. Moreover, the activation energy of RuO
2/MnO
2 was lower than commercial RuO
2 (19.53 kJ/mol). To know the active sites, cyclic voltammetry (CV) curve was tested with variation in scan rate (Fig. S8 in Supporting information). The double layer capacitance (
Cdl), estimated from slope of the plot of net current density versus scan rate, was 33.11 mF/cm
2 for RuO
2/MnO
2 (
Fig. 3d), promoted by 2.4-fold than RuO
2-300 deriving from the strain effect in the heterostructure with more defects [
24]. The estimation in catalytic performance of single catalytic center was conducted by means of normalization of OER performance with
Cdl. As shown in Fig. S9 (Supporting information), the specific activity was 1.43 A/F for RuO
2/MnO
2, enhanced by 1.2- and 1.1-time with relative to RuO
2-300 and benchmarked RuO
2, respectively. The higher specific catalytic activity was a distinct indicator of better intrinsic catalytic activity. The higher intrinsic catalytic activity was also testified by turnover frequency (TOF), which was 0.5 s
-1, 0.8 s
-1 and 4.3 s
-1 for RuO
2-300, commercial RuO
2 and RuO
2/MnO
2 at 1.6 V
vs. RHE, respectively. To confirm more active sites in RuO
2/MnO
2 compared to benchmarked RuO
2, the cyclic voltammetry curve was recorded from 0 V to 1.4 V
vs. RHE shown in
Fig. 3e. A clear anodic peak at 0.62 V
vs. RHE was detected for RuO
2/MnO
2 assigned to the oxidation of Ru
3+ to Ru
4+ structure due to more oxygen vacancies. Another oxidation peak at 1.31 V
vs. RHE was found due to the further oxidation of Ru
4+ to Ru
6+ specie [
25]. Although, this oxidation peak was more obvious for RuO
2/MnO
2; however, the peak ratio between Ru
4+ → Ru
6+ and Ru
3+ → Ru
4+ was lower for RuO
2/MnO
2 with relative to the counterpart of commercial RuO
2 revealing a lower percentage of Ru
4+ moieties have been oxidized; thereby, a higher structural stability was predicted. As deprotonation is involved in acidic OER process, the capability of deprotonation was estimated by Tafel slope of hydrogen desorption peak. As shown in Fig. S10 (Supporting information), Tafel slope was 451 mV/dec and 348 mV/dec for commercial RuO
2 and RuO
2/MnO
2, respectively, indicating a faster hydrogen desorption from RuO
2/MnO
2. To reveal the fast H desorption, the cyclic voltammetry curves were observed under various pH electrolyte (Fig. S11 in Supporting information). The plot of potential for H desorption
vs. pH was shown in
Fig. 3f, in which the slope was 54.5 mV/pH and 83.4 mV/pH for commercial RuO
2 and RuO
2/MnO
2. It is noted that 59 mV/pH indicates 1e
- and 1H
+ were involved in the reaction; thereby, in case of commercial RuO
2, 1e
-/1H
+ was involved for hydrogen desorption; however, 2e
-/3H
+ reaction was calculated for RuO
2/MnO
2, which would be due to the hydrogen spillover from active site to bridge oxygen (O
bri) and released from O
bri site. The OER performance was also recorded under different electrolyte with various pH values shown in Fig. S12 (Supporting information). As shown in
Fig. 3g, the reaction order of RuO
2/MnO
2 was 6.87, which was higher than commercial RuO
2 (5.02) suggesting the OER performance of RuO
2/MnO
2 was more sensitive to the hydrogen ion concentration. In RuO
2/MnO
2 structure, Ru-O
bri-Mn species were observed and the O
bri performed a better deprotonation capability since the deprotonation of absorbed *OOH species could be accelerated by the Mn atoms [
26]; thus, a better OER performance was achieved for RuO
2/MnO
2.