41 research outputs found
Effect of Temperature and Pressure on the Kinetics of the Oxygen Reduction Reaction
Fundamental
understanding of the oxygen reduction reaction in aqueous
medium at temperatures above 100 °C is lacking due to the practical
limitations related to the harsh experimental conditions. In this
work, the challenge to suppress water from boiling was overcome by
conducting the electrochemical investigation under pressurized conditions.
A striking improvement in the kinetics of the electrocatalytic reduction
of O<sub>2</sub> by about 150 fold relative to room temperature and
pressure was recorded under an O<sub>2</sub> pressure of 3.4 MPa at
200 °C in basic aqueous environment. To deconvolute the combined
effect of temperature and pressure, the underlying variables that
dictate the observed O<sub>2</sub> reduction kinetics of Pt and carbon
electrodes were examined individually. O<sub>2</sub> availability
at the electrode–solution interface was controlled by the interplay
between the diffusion coefficient and concentration of O<sub>2</sub>. Accurate knowledge of the temperature and pressure dependence of
O<sub>2</sub> availability at the electrode surface, the Tafel slope,
the transfer coefficient, and the electrochemical active surface area
was required to correctly account for the enhanced O<sub>2</sub> reduction
kinetics
High Activity Oxygen Evolution Reaction Catalysts from Additive-Controlled Electrodeposited Ni and NiFe Films
Electrodeposition
of Ni or NiFe films exhibiting fractal-like behavior
from plating baths containing an inhibitor, such as 3,5-diamino-1,2,4-triazole
(DAT), is found to yield oxygen evolution reaction (OER) catalysts
for alkaline solutions exhibiting high current densities (100 mA/cm<sup>2</sup>), high mass activity (∼1200 A/g of catalyst), high
stability (>72 h), and low overpotentials (∼300 mV). By
changing
electrodeposition time, the activity of the catalyst can be tuned,
with longer times yielding higher activities. The electrodeposition
method works with any conductive substrate yielding unprecedented
performance and providing an easy route to high activity catalysts
Origins of Less Noble Behavior by Au during CO Adsorption
The
behavior of the CO interaction with gold in an electrochemical
environment is presented in this work by means of the SERS technique.
The results show spectroscopic evidence that the adsorbed CO promotes
the formation of oxidic species even at potentials where it is not
thermodynamically favorable (lower than 0.6 V vs RHE), explaining
the low-overpotential CO electrooxidation reaction onset (@ ca. 0.2
V). At high potentials (<1.3 V), the CO displays an anomalous behavior,
persisting adsorbed on the surface at the high coverage oxide film,
which allows us to use the CO molecule as a probe and get information
about the electrode surface on the course of the reaction as well
as suggests gold oxide to be an active catalyst in small organic alcohol
oxidation
Elucidating Zn and Mg Electrodeposition Mechanisms in Nonaqueous Electrolytes for Next-Generation Metal Batteries
Cyclic
voltammetry and linear sweep voltammetry with an ultramicroelectrode
(UME) were employed to study Zn and Mg electrodeposition and the corresponding
mechanistic pathways. CVs obtained at a Pt UME for Zn electroreduction
from a trifluoromethylsulfonyl imide (TFSI<sup>–</sup>) and
chloride-containing electrolyte in acetonitrile exhibit current densities
that are scan rate independent, as expected for a simple electron
transfer at a UME. However, CVs obtained from three different Mg-containing
electrolytes in THF exhibit an inverse dependence between scan rate
and current density. COMSOL-based simulation suggests that Zn electrodeposition
proceeds via a simple one-step, two-electron transfer (E) mechanism.
Alternatively, the Mg results are best described by invoking a chemical
step prior to electron transfer: a chemical–electrochemical
(CE) mechanism. The chemical step exhibits an activation energy of
51 kJ/mol. This chemical step is likely the disproportionation of
the chloro-bridged dimer [Mg<sub>2</sub>(μ–Cl)<sub>3</sub>·6THF]<sup>+</sup> present in active electrodeposition solutions.
Our work shows that Mg deposition kinetics can be improved by way
of increased temperature
Mo-V‑O Based Electrocatalysts for Low Temperature Alcohol Oxidation
There
is a growing interest in alcohol oxidation electrochemistry
due to its role in renewable energy technologies. The goal of this
work was to develop active non- precious metal electrocatalysts based
on the Mo-V-(M)-O (M is Nb, Te) lattice. Selective gaseous alkane
oxidation had been previously observed on these catalysts at elevated
temperatures above 300 °C. In this study, the activity of the
catalysts at lower temperatures, 25–60 °C, was investigated.
Hydrothermal conditions were used to synthesize the Mo-V-(M)-O mixed
oxides. Physical characterization of the catalysts were obtained by
powder X-ray diffraction (XRD), scanning electron micrography (SEM)
equipped with energy dispersive X-ray (EDX), transmission electron
micrography (TEM), and X-ray photoelectron spectroscopy (XPS). The
catalytic activity for the oxidation of cyclohexanol was studied electrochemically.
Chronoamperometric studies were used to evaluate the long-term performance
of the catalysts. The onset of alcohol oxidative current was observed
between 0.2 and 0.6 V versus Ag/AgCl. Gas chromatography–mass
spectrometry analysis was used to determine the nature of the oxidative
products. The mild oxidation products, cyclohexanone and cyclohexene,
were observed after oxidation at 60 °C. The catalytic activity
increased in the order Mo-V-O < Mo-V-Te-O < Mo-V-Te-Nb-O. Mo-V-(Te,Nb)-O
based electrocatalysts efficiently catalyzed the oxidation of alcohols
at low temperatures
Effect of pH and Azide on the Oxygen Reduction Reaction with a Pyrolyzed Fe Phthalocyanine Catalyst
The active site of pyrolyzed Fe/N/C
electrocatalysts for the oxygen
reduction reaction (ORR) has been a source of debate since the initial
discovery that these materials demonstrated activity toward the ORR.
Here we utilize carbon-supported ironÂ(II) phthalocyanine (FePc) that
has been pyrolyzed at 800 °C in the absence and presence of azide
in acidic, neutral, and basic environments in order to probe the ORR
activity and mechanism of pyrolyzed Fe/N/C materials. The presence
of azide served to enhance the ORR activity of this material in neutral
electrolyte while having no effect in acid or base. Tafel slope differences
in addition to the azide enhancement suggest an iron-centered active
site for the ORR in pyrolyzed FePc and potentially other Fe/N/C electrocatalysts
ZnAl<sub><i>x</i></sub>Co<sub>2–<i>x</i></sub>O<sub>4</sub> Spinels as Cathode Materials for Non-Aqueous Zn Batteries with an Open Circuit Voltage of ≤2 V
Rechargeable
Zn batteries are promising energy storage alternatives
for Li-ion batteries in part because of the high specific and volumetric
capacities of Zn anodes, as well as their low cost, improved prospects
for safety, and the fact that they are environmentally friendly. Development
efforts, however, have focused mostly on aqueous electrolyte systems,
which are intrinsically limited by the narrow electrochemical potential
window of water. As a consequence, the use of alternative non-aqueous
electrolytes has attracted a growing level of interest with the hope
that they may provide higher operational voltages, which potentially
could provide viable pathways to high-energy and high-power density
Zn batteries. With regard to the latter, the considerable progress
made in developing useful non-aqueous electrolyte chemistries for
Zn anodes has not been matched by correlated progress regarding the
development of useful cathode materials. In this work, a new series
of spinels, ZnAl<sub><i>x</i></sub>Co<sub>2–<i>x</i></sub>O<sub>4</sub>, are reported and their utility as
cathode materials for non-aqueous Zn-ion batteries is demonstrated.
Full cells constructed using this new spinel as a cathode paired with
a metal anode showed capacities over 100 cycles of 114 mAh/g and an
onset potential of 1.95 V, which is the highest OCV yet reported for
a non-aqueous Zn-ion battery system. The data show that the Zn<sup>2+</sup> ions reversibly intercalate into the spinel structure during
the charge–discharge processes, a compositional transformation
directly correlated with a reversible conversion between Co<sup>4+</sup> and Co<sup>3+</sup> oxidation states within the lattice. The data
illustrate that the Al<sup>3+</sup>-doped spinel structure is a robust
candidate material for use in non-aqueous Zn batteries, suggesting
guidelines for the design of more efficient multivalent cathode materials
In Situ Raman Spectroscopy of Sulfur Speciation in Lithium–Sulfur Batteries
In situ Raman spectroscopy and cyclic
voltammetry were used to
investigate the mechanism of sulfur reduction in lithium–sulfur
battery slurry cathodes with 1 M lithium bisÂ(trifluoromethane sulfonyl)Âimide
(LiTFSI) and tetraethylene glycol dimethyl ether (TEGDME)/1,3-dioxolane
(DIOX) (1/1, v/v). Raman spectroscopy shows that long-chain polysulfides
(S<sub>8</sub><sup>2–</sup>) were formed via S<sub>8</sub> ring
opening in the first reduction process at ∼2.4 V vs Li/Li<sup>+</sup> and short-chain polysulfides such as S<sub>4</sub><sup>2–</sup>, S<sub>4</sub><sup>–</sup>, S<sub>3</sub><sup>•–</sup>, and S<sub>2</sub>O<sub>4</sub><sup>2–</sup> were observed
with continued discharge at ∼2.3 V vs Li/Li<sup>+</sup> in
the second reduction process. Elemental sulfur can be reformed in
the end of the charge process. Rate constants obtained for the appearance
and disappearance polysulfide species shows that short-chain polysulfides
are directly formed from S<sub>8</sub> decomposition. The rate constants
for S<sub>8</sub> reappearance and polysulfide disappearance on charge
were likewise similar. The formation of polysulfide mixtures at partial
discharge was found to be quite stable. The CS<sub>2</sub> additive
was found to inhibit the sulfur reduction mechanism allowing the formation
of long-chain polysulfides during discharge only and stabilizing the
S<sub>8</sub><sup>2–</sup> product
Exploring Salt and Solvent Effects in Chloride-Based Electrolytes for Magnesium Electrodeposition and Dissolution
We describe in this work Mg electrodeposition
and dissolution from
a wide range of inorganic ethereal electrolytes consisting of MgCl<sub>2</sub> and a second chloride salt. Systematic variations of the
cosalt reveal two broad classes of electrolytes, namely, the group
13 electrolytes, which require electrolytic cycling to improve their
performance, and electrolytes based on heavy p-block chlorides, which
exhibit Mg intermetallic formation. Results from electrospray ionization
mass spectrometry demonstrate that Mg deposition and stripping only
occur in electrolytes containing Mg multimers. We also explore the
role of solvent in determining the electrochemical performance of
chloride-based electrolytes. Our analysis establishes thermodynamic
parameters that dictate the ability of a solvent to support Mg electrochemistry
in the MgCl<sub>2</sub>–AlCl<sub>3</sub> system. In their totality,
these results illustrate important electrolyte design guidelines for
future Mg-ion batteries
<i>In Situ</i> Electrochemical Stress Measurements Examining the Oxygen Evolution Reaction in Basic Electrolytes
<i>In situ</i> electrochemical
stress measurements are
used to interrogate changes in oxide structure before and during the
oxygen evolution reaction (OER) from Ir, Ni, Co, Au, and Pt electrodes
in alkaline electrolyte. Stress evolution during potential cycling
reports on changes in oxidation state and oxide forms. Hysteresis
observed in the potential-dependent stress from Ir, Au, and Pt electrodes
is associated with chemical irreversibility in electrode composition
and roughness. Alternatively, Ni and Co exhibit reversible conversion
between hydroxide and oxyhydroxide forms during cycling. From the
experimentally determined stress, charge passed during electrode oxidation,
and Young’s modulus, the change in strain exhibited by Ni and
Co electrodes during hydroxide-oxyhydroxide conversion is calculated
to be 7.0% and 8.4%, respectively. We also show that the magnitude
of change in stress is proportional to the amount of material that
is further oxidized