Enhanced Electrochemical Catalytic Activity by Copper Oxide Grown on Nitrogen-doped Reduced Graphene Oxide

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Electronic Supporting Information Enhanced Electrochemical Catalytic Activity by Copper Oxide Grown on Nitrogen-doped Reduced Graphene Oxide Ruifeng Zhou, a,b Yao Zheng, a,b Denisa Hulicova-Jurcakova c and Shi Zhang Qiao *a a School of Chemical Engineering, the University of Adelaide, Adelaide, SA 00, Australia. Fax: +61 8 8303 4373; Tel: +61 8 8313 6443; E-mail: s.qiao@adelaide.edu.au b Australian Institute of Bioengineering and Nanotechnology, the University of Queensland, St Lucia, QLD 4072, Australia c School of Chemical Engineering, the University of Queensland, St Lucia, QLD 4072, Australia. 1 20 2 Chemicals All chemicals are purchased from Sigma-Aldrich and used without further treatment. Pt/C used is 20% Platinum on Vulcan XC-72, purchased from Fuel Cell Store. Syntehsis of GO Graphite flake (3 g) was put into concentrated H 2 SO 4 (12 ml), K 2 S 2 O 8 (2. g), and P 2 O (2. g). The mixture was kept at 80 C for 4. h, then cooled to room temperature and diluted with 0. L of DI water. The mixture was filtered and washed with DI water. The product was dried in vacuum at 0 C overnight. The pretreated graphite was put into cold (0 C) concentrated H 2 SO 4 (120 ml). Then, KMnO 4 (1 g) was added gradually under stirring and the temperature of the mixture was kept to be below 20 C by ice cooling. Successively, the mixture was stirred at 3 C for 2 h, and then diluted with DI water (20 ml) using ice bath cooling. The mixture was then stirred for 2 h, and then additional 0.7 L of DI water was added. 20 ml of 30% H 2 O 2 was added to the mixture. The mixture was washed with 1: HCl aqueous solution (1 L) and DI water. The resulting paste-like product was diluted to make a graphite oxide dispersion. Exfoliation was carried out by sonicating graphite oxide dispersion under ambient condition for 30 min, followed with centrifuging at 3000 rpm for 30 min to eliminate unexfoliated graphite. For measurement of N 2 adsorption-desorption isotherms, the GO is thermally reduced under 200 C 30 in vacuum to form rgo. 3 Synthesis of CuO 0.2 ml of 0.1 M CuCl 2 was added to 16 ml ethanol and stirred for min at 2 C. Then, 0.7 ml of 0.1 M NaOH was added to the suspension and stirred for another 1 hour. The suspension was then centrifuged, washed and dispersed in ethanol. Synthesis of CuO/GO. 0.2 ml of 0.1 M CuCl 2 was added to 8 ml of GO solution (1 mg ml -1 in water) and was stirred for min. Then 0.7 ml of 0.1 M NaOH was added to the suspension and stirred for another 1 hour at 60 C. The suspension was then centrifuged, washed with water and dispersed in ethanol. For measurement of N 2 adsorption-desorption isotherms, the sample is degased under 200 C in vacuum where GO is

thermally reduced to reduced GO (rgo). Characterization SEM images were taken with Philips XL30 FEG SEM. TEM images were collected with Tecnai F20. XRD spectrums were measured with Rigaku Miniflex benchtop XRD with Cu Kα line. N 2 adsorption/desorption measurement was carried out with Micromeritics Tristar II. Surface area is calculated by the multipoint BET method on basis of adsorption curve data. XPS were taken by KRATOS Axis Ultra DLD with Al Kα line. FTIR were collected with Nicolet 6700 FTIR. TGA were measured with SETARAM ABSYSTM Thermogravimetric Analysis. Formulae Koutecky-Levich equation: 1 J = 1 + 1 J L J K J is the measured current density. J L is the diffusion-limiting current density. J K is the kineticlimiting current density. J L = 0.62nFC 0 (D 0 ) 2/3 ν 1/6 ω 1/2 Where n is the electron transfer number, F = 9648 C mol -1 is Faraday constant, C 0 = 1.2 mol m -3 is the concentration of O 2, D 0 = 1.97-9 m 2 s -1 is the diffusion coefficient of O 2 in water, ν = 1.004-6 m2 s -1 1 is the kinematic viscosity of water, and ω is the angular velocity of the electrode. J K and n are derived from the slope and intercept of KL plot. Equation in RRDE Measurement: %HOO = 200 I r N I d + I r N 20 2 n = 4 I d I d + I r N I r is the ring current and I d is the disk current. N = 0.37 is the current collection efficiency of the RRDE. Calculation of equilibrium electrode potential of reaction (3) and (2*) All the equations and data from Ref. 1. Estimation of ionic activity coefficient In electrolyte of 0.1 M KOH and 0.01 M H 2 O 2, the concentrations of each kind of ions are: K + : 0.1 M, OH - : 0.09M, HOO - : 0.01M. The ionic strength (I) is estimated using equation:

I = 1 2 c iz i 2 Where c i and z i are the concentration and ionic charge of each ions. z i =1 for all ions so that I=0.1 for our electrolyte. Ionic activity coefficient of each ion (f i ) is calculated using Debye-Hückel equation: logf i = Az i 2 I 1 + Bå i I Where A and B are constants. At 2 C, A=0.11 and B=0.3291. å i is the effective radius of each ion in angstrom. For OH - and HOO -, å is taken 3.. As a result, f=0.761. Estimation of equilibrium electrode potential HOO + OH O 2 + H 2 O + 2e HOO + H 2 O + 2e 3OH E 3 Θ = 0.076V vs SHE E Θ 2 = 0.867V vs SHE 1 The equilibrium electrode potential of reaction is calculated by Nernst equation: E = E Θ + RT ZF lnq R=8.314 J K -1 mol -1 is the universal gas constant. T=298K is the absolute temperature. Z is the number of electrons involved in the electrode reaction. Z=2 for both reactions. F=9648 C mol -1 is the Faraday constant. Q is the reaction quotient. For reaction (3), pressure of O 2 is 1 atm. Thus [O 2 ] is 1. For reaction (2*): E 3 = E Θ 3 + RT ZF ln [O 2 ] [HO 2 ][OH = 0.021V vs SHE ] E 2 = E Θ 2 + RT ZF ln [HO 2 [OH = 0.908V vs SHE ] 3 The reference electrode used has potential 0.2 V vs SHE. Thus, Reference ] E 3 = 0.179V E 2 = 0.708V 1. Lange's Handbook of Chemistry, J. A. Dean, McGraw-Hill, Columbus, 1th edn., 1999, vol. 8, pp. 8.2-8., 8.132.

Supporting figures Fig. S1 SEM image of CuO/N-rGO. Micrometer-scale pores are shown. Fig. S2 XRD pattern of GO and N-rGO. High-shifted interplanar diffraction of N-rGO is attributed to decreased interplanar displacement by elimination of functional groups during reduction. Fig. S3 TGA of CuO/N-rGO in air. N-rGO is burnt out and CuO is remained.

Fig. S4 N 2 adsorption-desorption isotherms of GO and CuO/GO. Specific surface increases by CuO intercorporation. Fig. S FTIR of GO and N-rGO. Carboxyl groups are eliminated after reduction while hydroxyl groups remain. Fig. S6 High resolution XPS of O 1s of N-rGO. Carbonyl groups are of low amount after reduction.

Fig. S7 1st (solid) and 20 th (dash) CV of GO (a), CuO/GO (b), N-rGO (c) and CuO/N-rGO (d). GO is a poor in conductivity so that it shows very low capacitance. It is reduced at low potential and achieves high conductivity after 20 cycles of CV. N-rGO already has good conductivity but can still be reduced a bit. Fig. S8 LSV of Pt/C at different rotation rate (rpm).

Fig. S9 Electron transfer number of different catalysts calculated from RRDE test. The n is in accordance with that calculated from KL plot. 4 Current Density (ma cm -2 ) 2 0-2 MeOH injection Pt/C -4 CuO/NrGO 0 20 40 60 80 0 Time (s) Fig. S MeOH tolerance test of CuO/N-rGO and Pt/C under -0.3 V and 1600 rpm.