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. 2015 Mar 12;119(10):5467-5477.
doi: 10.1021/jp512311c.

Composite Ni/NiO-Cr2O3 Catalyst for Alkaline Hydrogen Evolution Reaction

Affiliations

Composite Ni/NiO-Cr2O3 Catalyst for Alkaline Hydrogen Evolution Reaction

Michael K Bates et al. J Phys Chem C Nanomater Interfaces. .

Abstract

We report a Ni-Cr/C electrocatalyst with unprecedented mass-activity for the hydrogen evolution reaction (HER) in alkaline electrolyte. The HER kinetics of numerous binary and ternary Ni-alloys and composite Ni/metal-oxide/C samples were evaluated in aqueous 0.1 M KOH electrolyte. The highest HER mass-activity was observed for Ni-Cr materials which exhibit metallic Ni as well as NiO x and Cr2O3 phases as determined by X-ray diffraction (XRD) and X-ray absorption spectroscopy (XAS) analysis. The onset of the HER is significantly improved compared to numerous binary and ternary Ni-alloys, including Ni-Mo materials. It is likely that at adjacent Ni/NiO x sites, the oxide acts as a sink for OHads, while the metallic Ni acts as a sink for the Hads intermediate of the HER, thus minimizing the high activation energy of hydrogen evolution via water reduction. This is confirmed by in situ XAS studies that show that the synergistic HER enhancement is due to NiO x content and that the Cr2O3 appears to stabilize the composite NiO x component under HER conditions (where NiO x would typically be reduced to metallic Ni0). Furthermore, in contrast to Pt, the Ni(O x )/Cr2O3 catalyst appears resistant to poisoning by the anion exchange ionomer (AEI), a serious consideration when applied to an anionic polymer electrolyte interface. Furthermore, we report a detailed model of the double layer interface which helps explain the observed ensemble effect in the presence of AEI.

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Figures

Figure 1
Figure 1
Diagnostic CV scans (50 mV/s) showing Hupd (+50 mV cathodic limit) and Hopd (−100 mV cathodic limit) on 50 μgPt/cm2 Pt/C (a) and 250 μgPt/cm2 unsupported Pt black (b) in the presence of Nafion vs AS-4 ionomer binders (incorporated during catalyst ink formulation). Scans collected in RDE cell with argon-purged 0.1 M KOH at 23 °C and 0 rpm.
Figure 2
Figure 2
CV scans (50 mV/s) showing HER activity on Pt/C (50 μgPt/cm2) and unsupported Pt black (250 μgPt/cm2) in the presence of Nafion vs AS-4 ionomer binder. Scans collected in RDE cell with argon-purged 0.1 M KOH at 23 °C and 2500 rpm.
Figure 3
Figure 3
Qualitative representation of electrostatic effects of AEI on φ1 and φ2. The condition studied previously under MOR conditions is represented in the top panel, while the condition studied in this paper is represented in the bottom panel. In both situations the chemical potential of the AEI (μAEI) increases the effective potentials at the IHP (φ1) and the OHP (φ2).
Figure 4
Figure 4
Steady-state HER chronoamperometry: 50 mV step size with 60 s hold-time/step in 0.1 M KOH (Ar-purged) at 50 °C and 2500 rpm. Catalyst loading is 50 μg(metal)/cm2 with 15 wt % AS-4 used as binder in catalyst layer.
Figure 5
Figure 5
CV showing HER kinetics of Pt (black), Ni–Cr/C (orange), 60% Ni/C (blue), and 60% Cr-Ox/C (red) catalysts in 0.1 M KOH (Ar-purged) at 50 °C and 2500 rpm with Nafion vs AS-4 binder tested in RDE cell. Ni–Cr/C (orange) is the only sample that exhibits increased HER activity in the presence of AEI. All samples were prepared with 50 μg/cm2 total metal loading.
Figure 6
Figure 6
XRD of 60% Ni–Cr/C sample. NiCr2O4 is mixture of NiO and Cr2O3. Peak positions of standards retrieved from ICDD ref: 01-070-0989 (Ni), 01-085-0936 (NiCr2O4), 00-004-0835 (NiO), 00-006-0504 (Cr2O3).
Figure 7
Figure 7
XANES (left) and FT-EXAFS (right) data at the Cr K edge collected on Ni–Cr/C electrodes. The data for Cr2O3 standard are also included for comparison purposes.
Figure 8
Figure 8
XANES (left) and FT-EXAFS (right) data at the Ni K edge collected on Ni–Cr/C electrodes. The XANES of Ni(OH)2 standard is also included for comparison purposes.
Figure 9
Figure 9
EXAFS fitting results from data collected from “original” Ni–Cr/C sample. Ni-edge fitting confirms mixture of metallic Ni0 and Ni-oxide. While Cr-edge fitting excludes the presence of NiCr2O4 since the Ni–metal bond (2.98 Å) is in agreement with that in Ni-oxide (2.95 Å in NiOx) but much smaller than the Ni–metal bond distance (3.42 Å) in NiCr2O4.
Scheme 1
Scheme 1
Proposed Interface Model for Alkaline HER on Pure Metal and M/MOx Surfacesa aAEI represented by archetypical quaternary ammonia polysulfone structure in OH-exchanged form. Metal represented by fcc unit cell model and metal oxide represented by NiO unit cell model.

References

    1. Carmo M, Fritz DL, Mergel J, Stolten D. A Comprehensive Review on Pem Water Electrolysis. Int. J. Hydrogen Energy. 2013;38:4901–4934.
    1. Kriston A, Xie T, Popov BN. Impact of Ultra-Low Platinum Loading on Mass Activity and Mass Transport in H2-Oxygen and H2- Air Pem Fuel Cells. Electrochim. Acta. 2014;121:116–127.
    1. Urian RC, Gullá AF, Mukerjee S. Electrocatalysis of Reformate Tolerance in Proton Exchange Membranes Fuel Cells: Part I. J. Electroanal. Chem. 2003:554–555. 307–324.
    1. Mukerjee S, Urian RC, Lee SJ, Ticianelli EA, McBreen J. Electrocatalysis of Co Tolerance by Carbon-Supported Ptmo Electro-catalysts in PEMFCs. J. Electrochem. Soc. 2004;151:A1094–A1103.
    1. Ehteshami SMM, Jia Q, Halder A, Chan SH, Mukerjee S. The Role of Electronic Properties of Pt and Pt Alloys for Enhanced Reformate Electro-Oxidation in Polymer Electrolyte Membrane Fuel Cells. Electrochim. Acta. 2013;107:155–163.