Supporting Information

Similar documents
ELECTRONIC SUPPLEMENTARY INFORMATION

Supporting Information. Christina W. Li and Matthew W. Kanan* *To whom correspondence should be addressed.

Supporting Information

Synthesis of Stable Shape Controlled Catalytically Active β-palladium Hydride

Electronic supplementary information. Efficient energy storage capabilities promoted by hierarchically MnCo 2 O 4

Supporting Information

Electronic Supplementary Information. for

Synthesis of Pt Ni Octahedra in Continuous-flow Droplet Reactors for the Scalable Production of Highly Active Catalysts toward Oxygen Reduction

Terephthalonitrile-derived nitrogen-rich networks for high

Comparison between the article and script of thesis

Synthesis and Evaluation of Electrocatalysts for Fuel Cells

Characteristic and efficiency of PEM fuel cell and PEM electrolyser

Preparation of Bi-Based Ternary Oxide Photoanodes, BiVO 4,

THE EFFECT OF ACETIC ACID ON THE INTEGRITY OF PROTECTIVE IRON CARBONATE LAYERS IN CO 2 CORROSION OF MILD STEEL

Tutorial Corrosion II. Electrochemical characterization with EC-Lab techniques

Supporting Information for Manuscript B516757D

Electricity. Characteristic and efficiency of PEM fuel cell and PEM electrolyser Stationary currents. What you need:

International Journal of Chemical Studies

Electrolysis, electrode polarisation, decomposition voltage, galvanic elements, Faraday s law.

ACCELERATED CORROSION TESTING OF GALVANIC COUPLES. James F. Dante, Josh Averett, Fritz Friedersdorf, and Christy Vestal

Mass Transport Effects on Electroreduction of Carbon Dioxide

Accelerated Stress Tests in PEM Fuel Cells: What can we learn from it?

Supporting Information. Low temperature synthesis of silicon carbide nanomaterials using

Corrosion Protect DLC Coating on Steel and Hastelloy

Supporting Information

PEFC cathode electrocatalysts: model system study

The electrodeposition of Zn-Mo and Zn-Sn-Mo alloys from citrate electrolytes

Novel concept of rechargeable battery using iron oxide nanorods. anode and nickel hydroxide cathode in aqueous electrolyte

Nanorods For Solar Water Oxidation.

Sealing of Hard Chrome Plating

1.Is the onsite potential affected by the voltage scanning rate? Or, is it a thermodynamically controlled process or kinetics dominant?

Cold Fusion at ENEA Frascati: Progress Report

Electrochemical Methods

Schottky Tunnel Contacts for Efficient Coupling of Photovoltaics and Catalysts

A Microfabricated Nickel-Hydrogen Battery Using Thick Film Printing Techniques. Ohio 44106, USA

Supplemental Information. A Low-Cost and High-Energy Hybrid. Iron-Aluminum Liquid Battery Achieved. by Deep Eutectic Solvents

Metallic 1T phase MoS 2 nanosheets as supercapacitor electrode materials

Corrosion Rate Measurement on C-Steel

Supporting Information. Epitaxial Growth of Twinned Au-Pt Core-Shell Star-Shaped. Decahedra as Highly Durable Electrocatalysts

ESFUELCELL MAXIMIZING THE USE OF PLATINUM CATALYST BY ULTRASONIC SPRAY APPLICATION

Supplementary Information

CHARACTARISTICS OF DAMAGE AND FRACTURE PROCESS OF SOLID OXIDE FUEL CELLS UNDER SIMULATED OPERATING CONDITIONS BY USING AE METHOD

Facile, mild and fast thermal-decomposition reduction of graphene oxide in air and its application in high-performance lithium batteries

Electronic Supplementary Material (ESI) for Chemical Communications This journal is The Royal Society of Chemistry 2013

Effect of Anodizing Potential on the Surface Morphology and Corrosion Property of AZ31 Magnesium Alloy

Twistable and Stretchable Sandwich Structured. Fiber for Wearable Sensors and Supercapacitors

for New Energy Materials and Devices; Beijing National Laboratory for Condense Matter Physics,

Supplementary Information

2 nd International Workshop on Degradation Issues of Fuel Cells Thessaloniki, Greece

Electrochemical properties of alkal. Citation Electrochimica Acta (2010), 55(3):

CuZn Alloy- Based Electrocatalyst for CO 2 Reduction. Thesis by. Amira Alazmi

Supplementary Material (ESI) for Chemical Communications. Solid-state single-crystal-to-single-crystal transformation from a 2D

Material-independent Fabrication of Superhydrophobic Surfaces by Musselinspired

ScienceDirect. Formation of Cu and Ni Nanowires by Electrodeposition

Development of Phosphoric Acid Fuel Cell Stack

NASF SURFACE TECHNOLOGY WHITE PAPERS 80 (7), 1-8 (April 2016) 10th Quarterly Report April - June 2015 AESF Research Project #R-117

Corrosion characteristics of mild steel in aqueous solution of formic acid containing some acetic acid

THE INFLUENCE OF ANODISING PARAMETERS ON THE CORROSION PERFORMANCE OF ANODISED COATINGS ON MAGNESIUM ALLOY AZ91D

Galvanic corrosion evaluation of 6061 aluminum coupled to CVD coated stainless steel Elizabeth Sikora and Barbara Shaw 6/9/2016

SPIRAL-WOUND PEM FUEL CELLS FOR PORTABLE APPLICATIONS. T.J. Blakley, K.D. Jayne, and M.C. Kimble

Electrocatalyst decorated hematite nanowire arrays for photoelectrochemical water splitting.

Laurea in Scienza dei Materiali Materiali Inorganici Funzionali. Electrolyzers

Application Note CORR-4

The effect of electroplating of Cr and Sn on corrosion resistance of low carbon steel (CK15)

P-6. Optimization of Citric Acid Passivation for Corrosion Resistance of Stainless Steel 440C. Chi Tat Kwok 1,2 and Wen He Ding 1.

Thin AC-PDP Vacuum In-line Sealing Using Direct-Joint Packaging Method

PEM Fuel Cell Accelerated Stress Tests and Durability Test Protocols. October 2014

Intrinsically Conductive Perovskite Oxides with Enhanced Stability and. Electrocatalytic Activity for Oxygen Reduction Reactions

Design and Development of Electro chromic Device using WO3 and Evaluation of its Optical and Thermal Properties

PVP-Functionalized Nanometer Scale Metal Oxide Coatings for. Cathode Materials: Successful Application to LiMn 2 O 4 Spinel.

Supplementary information. performance Li-ion battery

Supporting Information. Oxidation State of Cross-over Manganese Species on the Graphite Electrode of Lithium-ion Cells

Crystalline Thin Films: The Electrochemical Atomic Layer Deposition (ECALD) view. MMALEWANE MODIBEDI

Packaging Commercial CMOS Chips for Lab on a Chip Integration

Iron Cation Contamination Effect on the Performance and Lifetime of the MEA

EXCESS HEAT AND UNEXPECTED ELEMENTS FROM ELECTROLYSIS OF HEAVY WATER WITH TITANIUM CATHODES. R. Kopecek and J. Dash 1

Studies on Alloys and Composites that Undergo Anomalous Codeposition

CORROSION PROPERTIES OF CERMET COATINGS SPRAYED BY HIGH-VELOCITY OXYGEN-FUEL. Dragos UŢU, Iosif HULKA, Viorel-Aurel ŞERBAN, Hannelore FILIPESCU

Multipronged Characterization of the Corrosion Product Layer Formed on Mild Steel after Exposure to Acetic Acid

Production of Synthesis Gas by High-Temperature Electrolysis of H 2 O and CO 2 (Coelectrolysis)

Electronic Supplementary Information

ELECTROCHEMICAL SYNTHESIS OF POLYPYRROLE (PPy) and PPy METAL COMPOSITES ON COPPER and INVESTIGATION OF THEIR ANTICORROSIVE PROPERTIES

PULSED LASER WELDING

The Kinetic and Mechanism of The Oxygen Reduction Reaction on Pt, Au, Cu, PtCu/C and CuAu/C in Alkaline Media THESIS

CHAPTER-VII SUMMARY AND CONCLUSIONS

Electronic Supplementary Information. Minchan JEONG, Naoyoshi NUNOTANI, Naoki MORIYAMA, and Nobuhito IMANAKA

IRON CARBONATE SCALE GROWTH AND THE EFFECT OF INHIBITION IN CO 2 CORROSION OF MILD STEEL

Supplementary Materials: A Critical Evaluation of the Influence of the Dark Exchange Current on the Performance of Dye Sensitized Solar Cells

Development of microsensors for chloride concentration in concrete

FIOLAX. Solutions. Buffer solutions in the unique double-end ampoules offer a particularly high degree of reliability and measuring accuracy.

ONLINE MONITORING OF UNDERCOATING CORROSIONS UTILIZING COUPLED MULTIELECTRODE SENSORS. Xiaodong Sun Corr Instruments, LLC San Antonio TX, USA ABSTRACT

Supplementary Information.

Leveraging the Precision of Electroforming over Alternative Processes When Developing Nano-scale Structures

ELECTROCHEMICAL BEHAVIOURS OF LANTHANIDE FLUORIDES IN THE ELECTROLYSIS SYSTEM WITH LiF-NaF-KF SALT

Nickel Electroplating

Oxygen reduction characteristics of several valve metal oxide electrodes in HClO 4 solution

Low Cost Bipolar Plates for Large Scale PEM Electrolyzers

Method of converting nitrogen dioxide to nitric oxide

Pressure & Vacuum Measurement. Solutions. Series 274

Transcription:

Supporting Information Copyright Wiley-VCH Verlag GmbH & Co. KGaA, 69451 Weinheim, 2014 Discovery of New Oxygen Evolution Reaction Electrocatalysts by Combinatorial Investigation of the Ni La Co Ce Oxide Composition Space Joel A. Haber, [a] Dan Guevarra, [a] Suho Jung, [a] Jian Jin, [b] and John M. Gregoire* [a] celc_201402149_sm_miscellaneous_information.pdf

Table of Contents Materials and Methods Preparation of Pseudo-quaternary Library p. 2 Preparation of Ni 0.1 La 0.1 Co 0.3 Ce 0.5 O x Catalyst on Glassy Carbon p. 2 Electrochemical Characterization with Scanning Electrochemical Drop Cell p. 3 Electrochemical Characterization with Glassy Carbon RDEs p. 3 SEM and EDS Characterization of the Library and Glassy Carbon RDEs p. 5 XPS Characterization of Catalyst film on Glassy Carbon p. 5 Figure S1 p. 6 Figure S2 p. 7 Figure S3 p. 8

Materials and Methods Sample Preparation (for 5.0 at% library). The discrete pseudo-quaternary (Ni-La-Co-Ce)O x library was designed as an array with 5.0 at% composition steps for each of Ni, La, Co, and Ce. The complete array of 1771 samples was deposited by inkjet printing onto the FTO-coated side of a 10 cm x 15 cm glass plate at a resolution of 2880 x 1440 dpi (21, 22). Four separate metal inks, of the type previously described by Fan and Stuckey,[8] were prepared by mixing 5 mmoles of each of the Ni, La, Co, and Ce precursor with 0.80 g Pluronic F127 (Aldrich), 1.0 ml glacial acetic acid (T.J. Baker, Inc.) ( 0.2 ppm Fe), 0.40 ml of concentrated HNO 3 (EMD) ( 0.2 ppm Fe), and 30 ml of 200 proof Ethanol (Koptec). The metal precursors were Ni(NO 3 ) 2-6H 2 O(1.56 g, 98.5%, 10 ppm Fe, Sigma Aldrich), La(NO 3 ) 3-6H 2 O (2.19 g, 99.999%, 10 ppm Fe, Sigma Aldrich), Co(NO 3 ) 2-6H 2 O (1.49 g, 99.999%, 2.1 ppm Fe, Sigma Aldrich), and Ce(NO 3 ) 3-6H 2 O (2.47 g, 99.99%, 5 ppm Fe, Sigma Aldrich). After printing the library of compositions as a set of 1 mm x 1 mm spots on a 2 mm pitch, the inks were dried and the metal precursors converted to oxides by calcination in air at 40 C for 18 h, then at 70 C for 24 h, followed by a 5 h ramp and 10 h soak at 350 C. The ink formulation and thermal processing protocol maintains intimate mixing of the precursors up to the final calcination step, during which the thermodynamics of the produced mixed metal oxides influences the final structure. Preparation of Catalyst on Glassy Carbon. The selected composition (Ni 10 La 10 Co 30 Ce 50 ) was printed onto glassy carbon rotating disk electrodes (GC RDEs, SIGRADUR G, HTW Hochtemperatur-Werkstoffe GmbH), which are cylinders 5 mm in diameter and 4 mm in height. Four separate metal inks were prepared as described above and printed at 2880 x 1440 dpi, at 7.5 nmoles of metal per mm 2. After printing, the inks were dried and the metal precursors 2

converted to oxides using the same calcination and annealing process used for the combinatorial library. Electrochemical Characterization Scanning droplet photoelectrochemical cell. The detailed geometry and operational performance of a scanning droplet cell were described by Gregoire, et. al. [3b] Briefly, a drop of solution was formed on top of a 1 mm x 1 mm ink-jet printed sample. The shape of the droplet was directed and controlled by a solution inlet port and multiple solution outlet ports without the need for a sealing gasket. The scanning droplet cell (SDC) provided an individual 3-electrode cell for each sample, including a capillary Ag/AgCl reference electrode terminating within 1 mm of the sample surface and a platinum wire counter electrode placed in the solution influent. In this study, we continuously supplied an oxygen-saturated 1.0 M NaOH(aq) solution to form a drop contact to each catalyst sample, which in this SDC configuration produces an uncompensated resistance of approximately 15 Ω. After moving to a new sample location, a 2 second cell stabilization period preceded the electrochemical experiments, which included a 15 s CP measurement at current density J = 10 ma cm -2 followed by a CV at 100 mv s -1 from -60 mv to 480 mv overpotential for the OER reaction. The catalyst overpotential was determined using the final measured potential of the CP measurement, creating the compositional maps of catalyst performance shown in Figures 1 and S1. Visual inspection of representative CP data confirmed that the overpotential stabilized within 5 mv by the end of the 15 s measurement. Electrochemical analysis of catalysts on glassy carbon rotating disk electrodes. GC RDE electrodes coated with each composition were subjected to a series of electrochemical measurements in oxygen-saturated 1.0 M NaOH (prepared from millipure H 2 O and NaOH 3

pellets, 98%, 5 ppm Fe, Sigma Aldrich Bio Ultra) blanketed under 1 atm O 2 (g). The working electrode was rotated at 1600 rpm and the counter and reference electrodes were a carbon rod (99.999%, Alfa Aesar), and a commercial saturated calomel electrode (SCE) (CH-Instruments), respectively. All measurements were conducted in a modified two-chamber U-cell in which the first chamber held the working and reference electrodes in ca. 120 ml of solution, and the second chamber held the auxiliary electrode in ca. 25 ml. The two chambers were separated by a fineporosity glass frit. The cell was purged for ca. 20 min with O 2 prior to each set of experiments. During static-voltammetry measurements, the solution in the first chamber was blanketed under O 2. During rotating-disk electrode voltammetry measurements, the solution in the first chamber was continuously bubbled with O 2. The uncompensated resistance of the cell was measured with a single-point high-frequency impedance measurement and IR drop was compensated at 85% through positive feedback using the Bio-Logic EC-Lab software. The typical electrochemical cell had uncompensated resistance of approximately 20 Ω in 1 M NaOH. Each catalyst was investigated by a CV at 10 mv s -1 (forward and reverse sweep shown in Figure 2c), a series of 30 second controlled-current CP steps and a series of controlled-potential CA steps (shown in Figure 2a), and a 120 minute CP measurement at 10 ma/cm 2 current density (shown in Figure 2b). The quasi-steady state CP and CA measurements in Figure 2 do not contain appreciable sample oxidation current and thus follow the Tafel trend. At high- the data deviate from the exponential behavior, possibly due to bubble formation at the electrode surface and corresponding decrease in electrochemically accessible surface area. 4

SEM and EDS Characterization of the Library and Glassy Carbon RDEs. Select catalysts in the library were characterized using bulk composition measurements (energy dispersive x-ray spectroscopy, EDS), as reported in Table S1. The EDS analysis demonstrates reasonable fidelity between the measured and intended compositions; however, the measured concentration for La is somewhat lower than intended. The discrepancies are on the order of the general EDS accuracy of 10% and we additionally note that the Ce-K and La-K peaks are strongly overlapped, creating the possibility of systematic quantification errors. Alternatively, the printed La concentrations could in fact be lower than intended due to poor control of the La concentration in the ink. The precursor La(NO 3 ) 3 salt is hygroscopic, confounding the measurement of precursor mass during ink preparation. The deviation from intended La concentration does not affect the discovery of new active composition regions. In this paper all compositions reported are the intended compositions, except where EDS measurements are noted. Pre- and post-stability test examination of the electrodes by SEM was performed and is summarized in Figure S2. The composition intended to be deposited on the GC RDEs was Ni 0.1 La 0.1 Co 0.3 Ce 0.5. The measured EDS compositions of the corresponding RDE sample was Ni 0.12 La 0.07 Co 0.36 Ce 0.45 as-prepared and Ni 0.12 La 0.07 Co 0.31 Ce 0.50 after the extensive electrochemical testing. The decrease in Co concentration after the 2 h stability test may be related to selective dissolution or to the flaking of regions of catalyst film observed by SEM (see Figure S2). No Fe was detected by EDS in any samples examined. XPS of Catalyst films on Glassy Carbon Disks. XPS survey scans were collected of the asprepared films (before electrolysis) to check for Fe impurities. XPS data was collected using a Kratos Axis Nova with monochromatic Al Kα excitation at 1486 ev and 150W power. Experiments were performed at the base pressure of 10-9 Torr. The data were collected at 160 ev 5

pass energy with an energy resolution of about 1.5 ev. No Fe was detected in these survey scans. Table S1. Comparison of intended compositions with compositions measured by EDS for all 50:50 bimetallic composition samples. Target compositions Measured compositions Ni La Co Ce Ni La Co Ce 0.5 0 0.5 0 0.48 0.01 0.49 0.03 0.5 0.5 0 0 0.54 0.4 0.05 0 0 0.5 0.5 0 0 0.38 0.61 0 0 0 0.5 0.5 0 0.02 0.46 0.52 0 0.5 0 0.5 0.02 0.4 0.01 0.57 0.5 0 0 0.5 0.51 0 0.02 0.47 Figure S1. Performance map of (Ni-La-Co-Ce)O x oxygen evolution catalysts. The overpotential required for performing oxygen evolution at 10 ma cm -2 is shown as a function of physical position in the combinatorial library. 6

Before Electrochemical testing After electrochemical testing Figure S2. SEM/EDS characterization of the Ni 0.1 La 0.1 Co 0.3 Ce 0.5 O x catalyst on glassy carbon RDE electrodes before and after the standardized electrochemical testing protocol. 7

After calcination the catalyst film is cracked, with submicron gaps between film segments and with some regions of bare glassy carbon where the film flaked off. After the 2 h stability test, it is apparent that additional 10-20 micron diameter flakes of the cracked film have been removed, leaving dark black outlines on the glassy carbon surface. EDS confirms that only C, and no Ni, La, Co, or Ce were present on these dark regions. During the stability testing protocol the electrodes are rotated at 1600 rpm, and the associated hydrodynamic forces are apparently sufficient to delaminate some of the film flakes. After this initial mechanical failure, the remaining film is stable, as indicated by the stable CP trace in Figure 2b. Figure S3. Voltage required to drive the electrolysis of water for 100 hours in a testbed two compartment electrolyzer at 20 ma (4.0-4.5 ma/cm 2 current density). The broad peaks in potential result from changes in fill level of the 1 M NaOH(aq) electrolyte, when refilled the active surface area was increased and the potential dropped abruptly. The sharp peaks in voltage result from momentary loss of electrical contact to the electrolyzer. 8