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Fast operational mode switching effects on battery degradation

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Abstract

Conventions established for battery cycling were originally from the domain of chemists and material scientists interested in characterizing the battery materials. Involvement in studies with large energy storage batteries for residential energy systems outfitted with renewables demonstrated that such scenarios were very different compared to cycling regimes used for battery characterization. Transient, irregular power production and storage coupled with stochastic electrical demand result in battery usage where frequent switching between charge and discharge modes occurs. Further, energy storage control systems favor maintaining the battery in an elevated state of charge. In view of these different circumstances, experiments to characterize battery performance for a more generalized and comprehensive operating environment were developed which explored varying amplitudes of battery cycles, as well isolating a full range of instantaneous depth of discharge levels with very small amplitude cycles. To investigate the operations on a mechanistic level, numerical simulations with a pseudo-2D electrochemical model were run to discover what is occurring inside the electrodes under these conditions. It was found that localized degradation effects vary significantly across the battery capacity range, and that the net extent of degradation increased with the duration of uninterrupted charging or discharging. Analysis was performed to find a good correlation between the measured cell degradation with time-dependent transport of electrolyte phase lithium ions in the anode as a driver for SEI formation. These findings have some bearing on claims being made about pulse charging regimes under development aimed at allowing fast charging with minimal cell capacity loss penalties.

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Abbreviations

\(c_{\mathrm {max}E}\) :

Li concentration in electrolyte phase (mol m−3)

\(c_{\mathrm {max}S}\) :

Li concentration at electrode surface (mol m−3)

\(c_{{{\text{excess}}{\kern 1pt} i}}\) :

Excess transported lithium-ion flux (mol m−2 s−1)

\(C_A\) :

Reagent concentration in Eq. 6 (mol m−3)

\(C_S\) :

Surface site concentration in Eq. 6 (mol m−2)

C :

Characteristic cell current for a one-hour discharge (A)

\(\hbox {cap}_\mathrm {fade}\) :

Battery cell capacity loss (A h)

D :

Diffusivity constant for SEI layer (m2 s−1)

\(D_E\) :

Diffusivity constant for lithium in electrolyte medium (m2 s−1)

\(D_S\) :

Diffusivity constant for lithium in electrode material (m2 s−1)

f :

Ionic activity factor, used here in \(\frac{d \ln f}{d \ln c_E}\) which \(\approx 0\) [29]

F :

Faraday constant = 28.601 (A h mol−1)

\(i_0\) :

Exchange current density for intercalation (A m−2)

I :

Cell current (A)

j :

Intercalation current density (A m−2)

k :

Kinetic coefficient in Eqs. 4 and 6 (m2 s−1)

\(k_0\) :

Proportionality constant in Eq. 3 (m2 s−1)

L :

SEI layer thickness (m)

m :

Molecular mass of SEI material (kg mol−1)

\(Q_D\) :

Rated discharge capacity of a cell (A h)

r :

General surface reaction rate (mol m−3 s−1)

R :

Universal gas constant = 8.3144 (J mol-1 K−1)

R :

In Fig. 5 and Table 1, particle radius in electrode compact (m)

\(S_a\) :

Electrode specific surface area (m2 m−3)

t :

Time (s)

\(t^{0}_{+}\) :

Ion transport number (–)

T :

Temperature (K)

V cell :

Compute cell volume (m3)

x :

Spatial dimension in battery domain (m)

\(\gamma\) :

Temperature factor exponent (–)

\(\kappa\) :

Ionic conductivity of electrolyte (S m−1)

\(\phi\) :

Electrode potential (V)

\(\eta\) :

Electrode overpotential (V)

\(\rho\) :

Density of SEI layer (kg m−3)

\(\sigma\) :

Electrode conductivity (S m−1)

app:

The external applied load for electric current

CUR:

Battery current

DOD:

Battery depth of discharge

E :

Electrolyte phase

REF:

Reference conditions

S :

Solid (electrode) phase

1,2,-1:

Reaction step index in Eq. 6

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Acknowledgements

Funding for this work was provided through the Program of Energy Research and Development (PERD) at Natural Resources Canada, and the project was commissioned by the Vehicle Propulsion Technology program of the National Research Council of Canada.

Funding

Funding was provided by PERD (Grant No. TR2-3B02.003).

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Correspondence to K. Darcovich.

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Darcovich, K., Recoskie, S. & Fattal, F. Fast operational mode switching effects on battery degradation. J Appl Electrochem 50, 111–124 (2020). https://doi.org/10.1007/s10800-019-01373-4

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