43 research outputs found
Attainable Gravimetric and Volumetric Energy Density of Li–S and Li Ion Battery Cells with Solid Separator-Protected Li Metal Anodes
As
a result of sulfur’s high electrochemical capacity (1675
mA h/g<sub>s</sub>), lithium–sulfur batteries have received
significant attention as a potential high-specific-energy alternative
to current state-of-the-art rechargeable Li ion batteries. For Li–S
batteries to compete with commercially available Li ion batteries,
high-capacity anodes, such as those that use Li metal, will need to
be enabled to fully exploit sulfur’s high capacity. The development
of Li metal anodes has focused on eliminating Coulombically inefficient
and dendritic Li cycling, and to this end, an interesting direction
of research is to protect Li metal by employing mechanically stiff
solid-state Li<sup>+</sup> conductors, such as garnet phase Li<sub>7</sub>La<sub>3</sub>Zr<sub>2</sub>O<sub>12</sub> (LLZO), NASICON-type
Li<sub>1+<i>x</i></sub>Al<sub><i>x</i></sub>Ti<sub>2–<i>x</i></sub>(PO<sub>4</sub>)<sub>3</sub> (LATP),
and Li<sub>2</sub>S–P<sub>2</sub>S<sub>5</sub> glasses (LPS),
as electrode separators. Basic calculations are used to quantify useful
targets for solid Li metal protective separator thickness and cost
to enable Li metal batteries in general and Li–S batteries
specifically. Furthermore, maximum electrolyte-to-sulfur ratios that
allow Li–S batteries to compete with Li ion batteries are calculated.
The results presented here suggest that controlling the complex polysulfide
speciation chemistry in Li–S cells with realistic, minimal
electrolyte loading presents a meaningful opportunity to develop Li–S
batteries that are competitive on a specific energy basis with current
state-of-the-art Li ion batteries
Quantification of Surface Oxygen Depletion and Solid Carbonate Evolution on the First Cycle of LiNi<sub>0.6</sub>Mn<sub>0.2</sub>Co<sub>0.2</sub>O<sub>2</sub> Electrodes
By combining differential
electrochemical mass spectrometry (DEMS) with titrations of electrochemically
modified LiNi0.6Mn0.2Co0.2O2 (NMC622), we find that
coinciding with the onset of CO2 evolution above ∼3.9
V vs Li/Li+ anodic cutoff potentials are several phenomena:
(i) degradation of the native surface Li2CO3, (ii) degradation of the electrolyte evolving CO2, (iii)
formation of a film of carbonate-like electrolyte degradation products
on charge which are (iv) largely reduced and desorb on discharge,
(v) near-surface oxygen charge compensation during charge, and (vi)
irreversible formation of a transition metal-reduced, oxygen-depleted
layer on the surface of NMC622 that persists after discharge. CO2 stemming from electrolyte degradation and Li2CO3 decomposition begins to evolve above ∼3.9 V on charge,
discharge, and rest and results from a corrosion-like process involving
NMC622, which appears to be distinct from the process that evolves
O2. As measured using titrations that quantify surface
peroxo-like character, the disordered surface layer that forms during
cycling extends deeper into the oxide bulk than would be anticipated
simply from the total O2 evolved. The analyses we report
here could be used to quantify the role of the electrolyte, surface
contaminants, and transition metal oxide composition on outgassing,
electrolyte decomposition, and transition metal oxide surface degradation
The Sudden Death Phenomena in Nonaqueous Na–O<sub>2</sub> Batteries
Metal–air
(O<sub>2</sub>) batteries have been intensely
studied over the past decade as potential high-energy alternatives
to current state-of-the-art Li-ion batteries. Although Li–O<sub>2</sub> batteries possess higher theoretical specific energies, Na–O<sub>2</sub> cells have been reported to achieve higher capacities on
discharge and exhibit much lower overpotentials on charge than analogous
Li–O<sub>2</sub> cells. Nevertheless, sudden and large overpotential
increases (“sudden deaths”) occur in Na–O<sub>2</sub> cells on both discharge and charge, substantially limiting
achievable capacity on discharge and increasing the average charge
voltage, thereby reducing round-trip energy efficiency. In this work,
we unravel the origins of these sudden death phenomena, which have
been previously linked to the electrochemistry occurring at the cathode.
On discharge, the maximum capacity was limited by pore clogging at
low current densities and by surface passivation at high current densities,
with concentration polarization playing only a small role in limiting
the achievable capacity. On charge, the discharge and charge current
densities were both found to influence the attainable capacity prior
to sudden death. We propose a charge mechanism consistent with our
data, where a concerted surface oxidation mechanism and a dissolution–oxidation
mechanism both contribute to the observed overpotentials. Sudden death
on charge is proposed to occur when these two pathways cannot support
the applied current rate
Ion Transport in (Localized) High Concentration Electrolytes for Li-Based Batteries
High concentration
electrolytes (HCEs) and localized high concentration
electrolytes (LHCEs) have emerged as promising candidates to enable
higher energy density Li-ion batteries due to their advantageous interfacial
properties that result from their unique solvent structures. Using
electrophoretic NMR and electrochemical techniques, we characterize
and report full transport properties, including the lithium transference
numbers (t+) for electrolytes ranging
from the conventional ∼1 M to HCE regimes as well as for LHCE
systems. We find that compared to conventional electrolytes, t+ increases for HCEs; however the addition of
diluents to LHCEs significantly decreases t+. Viscosity effects alone cannot explain this behavior. Using Onsager
transport coefficients calculated from our experiments, we demonstrate
that there is more positively correlated cation–cation motion
in HCEs as well as fast cation–anion ligand exchange consistent
with a concerted ion-hopping mechanism. The addition of diluents to
LHCEs results in more anticorrelated motion indicating a disruption
of concerted cation-hopping leading to low t+ in LHCEs
Counterion Transport and Transference Number in Aqueous and Nonaqueous Short-Chain Polyelectrolyte Solutions
Nonaqueous polyelectrolyte solutions have recently been
proposed
as potential battery electrolytes due to their unique ability to tune
the mobility of the anion relative to that of the electrochemically
active lithium ion. This could potentially be used to study the effect
of concentration polarization during battery charge, a major limiting
factor in achieving fast charge rates that is caused by high anion
mobility. An important consideration in the design of polyelectrolyte
solutions for battery applications is the solubility of the polymer
in battery-relevant carbonate blend solvents. Little is understood
from a transport perspective, however, about the importance of designing
the polymer to be solvophillic or if it is sufficient to obtain solubility
through the incorporation of appended ions alone (as with polystyrene
sulfonate in water). Using a model polysulfone-based system without
added salt, we investigate the conductivity, viscosity, and diffusion
of polyelectrolyte solutions over a range of concentrations and molecular
weights in dimethyl sulfoxide (DMSO) and water. In both solvents,
sulfonated polysulfone is readily soluble and the charged group is
known to dissociate, but the neutral backbone polymer is only soluble
in DMSO. We find marked differences in the transport behavior of polymer
solutions prepared from the two solvents, particularly at high concentrations.
Comparing this transport behavior to that of the monomer in solution
demonstrates a larger decrease in lithium motion in DMSO than in water,
even though the bulk viscosity in water increases far more rapidly.
This study sheds light on the important parameters for optimizing
polyelectrolyte solution transport in different solvents
Altering Surface Contaminants and Defects Influences the First-Cycle Outgassing and Irreversible Transformations of LiNi<sub>0.6</sub>Mn<sub>0.2</sub>Co<sub>0.2</sub>O<sub>2</sub>
By altering the surface
of LiNi0.6Mn0.2Co0.2O2 (NMC622) we show that surface defects and contaminants dominate
the outgassing and irreversible surface transformations during the
first electrochemical cycle. To alter the surface defects and contaminants
without changing the bulk structure of the NMC622, we perform mild
methanol and water rinses, a water soak, a water rinse and subsequent
heat treatment, as well as purposeful increase of the surface Li2CO3. By combining isotopic labeling; gas analysis;
and peroxide, hydroxide, and carbonate titrations we observe that
these alterations change the surface Li2CO3,
surface hydroxides, and the local defects, which in turn alter the
nature and extent of the outgassing to O2 and CO2. Our results highlight that outgassing of Li-ion cathode materials
is highly dependent on the synthesis and storage routes and comparison
of varying compositions must take into account these differences to
make any meaningful conclusions. We also show that simple rinsing
procedures may be an effective route to controlling interfacial reactivity
of Li-ion active materials
Lithium-Ion Transport and Exchange between Phases in a Concentrated Liquid Electrolyte Containing Lithium-Ion-Conducting Inorganic Particles
Understanding Li+ transport in organic–inorganic
hybrid electrolytes, where Li+ has to lose its organic
solvation shell to enter and transport through the inorganic phase,
is crucial to the design of high-performance batteries. As a model
system, we investigate a range of Li+-conducting particles
suspended in a concentrated electrolyte. We show that large Li1.3Al0.3Ti1.7P3O12 and Li6PS5Cl particles can enhance the overall
conductivity of the electrolyte. When studying impedance using a cell
with a large cell constant, the Nyquist plot shows two semicircles:
a high-frequency semicircle related to ion transport in the bulk of
both phases and a medium-frequency semicircle attributed to Li+ transporting through the particle/liquid interfaces. Contrary
to the high-frequency resistance, the medium-frequency resistance
increases with particle content and shows a higher activation energy.
Furthermore, we show that small particles, requiring Li+ to overcome particle/liquid interfaces more frequently, are less
effective in facilitating Li+ transport. Overall, this
study provides a straightforward approach to study the Li+ transport behavior in hybrid electrolytes
Chemical and Electrochemical Differences in Nonaqueous Li–O<sub>2</sub> and Na–O<sub>2</sub> Batteries
We present a comparative study of nonaqueous Li–O<sub>2</sub> and Na–O<sub>2</sub> batteries employing an ether-based electrolyte. The most intriguing difference between the two batteries is their respective galvanostatic charging overpotentials: a Na–O<sub>2</sub> battery exhibits a low overpotential throughout most of its charge, whereas a Li–O<sub>2</sub> battery has a low initial overpotential that continuously increases to very high voltages by the end of charge. However, we find that the inherent kinetic Li and Na–O<sub>2</sub> overpotentials, as measured on a flat glassy carbon electrode in a bulk electrolysis cell, are similar. Measurement of each batteries’ desired product yield, <i>Y</i><sub>NaO2</sub> and <i>Y</i><sub>Li2O2</sub>, during discharge and rechargeability by differential electrochemical mass spectrometry (DEMS) indicates that less chemical and electrochemical decomposition occurs in a Na–O<sub>2</sub> battery during the first Galvanostatic discharge–charge cycle. We therefore postulate that reactivity differences (Li<sub>2</sub>O<sub>2</sub> being more reactive than NaO<sub>2</sub>) between the major discharge products lead to the observed charge overpotential difference between each battery
Inherent Acidity of Perfluorosulfonic Acid Ionomer Dispersions and Implications for Ink Aggregation
Perfluorosulfonic
acid (PFSA) dispersions are used as components
in a variety of electrochemical technologies, particularly in fuel-cell
catalyst-layer inks. In this study, we characterize dispersions of
a common PFSA, Nafion, as well as inks of Nafion and carbon. It is
shown that solvent choice affects a dispersion’s measured pH,
which is found to scale linearly with Nafion loading. Dispersions
in water-rich solvents are more acidic than those in propanol-rich
solvents: a 90% water versus 30% water dispersion can have up to a
55% measured proton deviation. Furthermore, because electrostatic
interactions are a function of pH, these differences affect how particles
aggregate in solution. Despite having different water contents, all
inks studied demonstrate the same particle size and surface charge
trends as a function of pH, thus providing insights into the relative
influence of solvent and pH effects on these properties
Oxygen Pressure Influences Spatial NaO<sub>2</sub> Deposition and the Sudden Death Mechanism in Na–O<sub>2</sub> Batteries
Over the past decade, metal–O<sub>2</sub> batteries have been intensely studied as potential high energy
density alternatives to current state-of-the-art Li-ion batteries.
Of these, nonaqueous Na–O<sub>2</sub> batteries offer high
stability, improved full-cycle efficiency, and lower overpotentials,
particularly on charge, when compared to the higher-energy-density
Li–O<sub>2</sub> system. However, Na–O<sub>2</sub> batteries
exhibit sudden and large overpotential increases or “sudden
deaths” on discharge, substantially limiting the achievable
capacity. In this work, we examine the influence of O<sub>2</sub> pressure
effects in Na–O<sub>2</sub> batteries and the mechanism of
sudden death at different O<sub>2</sub> pressures and current density
regimes. We observe that at a given current density, there exists
a transition between failure mechanisms with O<sub>2</sub> pressure
as a result of different phenomena related to the deposition of the
solid discharge product, sodium superoxide (NaO<sub>2</sub>). Cells
operated at a lower O<sub>2</sub> pressure are more susceptible to
failure due to surface passivation resulting from thin NaO<sub>2</sub> film coverage, whereas cells operated at a higher O<sub>2</sub> pressure
achieve higher capacities but are increasingly subject to failure
due to pore clogging from substantial solid NaO<sub>2</sub> deposition.
We associate the transition between these failure mechanisms with
a combination of electron and mass transfer effects, leading to dramatic
differences in the spatial deposition of NaO<sub>2</sub> through the
cathode
