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V. Focused Fundamental Research - EERE - U.S. Department of ...

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V.E.4 Mathematical Modeling <strong>of</strong> Next-generation Li-ion Chemistries (LBNL)<br />

Srinivasan – LBNL<br />

Particle size study on LiFePO 4 cathodes. For studying<br />

the effect <strong>of</strong> particle size distribution in the LiFePO 4<br />

system, a porous electrode model that incorporates<br />

transport in both the solid and electrolyte phases along<br />

with two particles sizes was developed. The LiFePO 4<br />

system is characterized by its flat equilibrium potential.<br />

The equilibrium potential was obtained by measuring the<br />

open-circuit potential after discharging the electrode at a<br />

slow rate to a certain SOC. The measured equilibrium<br />

potential was applied in the porous electrode model to 4.2<br />

calculate the electrode potentials during charge and<br />

discharge.<br />

4.0<br />

Stress studies on graphite anodes. A single particle<br />

with a layer <strong>of</strong> binder was used to study the mechanical<br />

degradation <strong>of</strong> battery anodes. Equations were developed<br />

for stress generation in the particle and the interaction <strong>of</strong><br />

stress in the active material with that in the binder. The<br />

model also considers the volume changes in the active<br />

increasing SOC also explains the asymmetry <strong>of</strong> electrode<br />

utilization between charge and discharge as seen in Figure<br />

2. The strong dependency <strong>of</strong> Li diffusion coefficient on its<br />

concentration suggests that the use <strong>of</strong> a varying diffusion<br />

coefficient is necessary for studying the transport<br />

processes in insertion materials and for further application<br />

to the macroscopic porous electrode.<br />

Potential (V) vs. Li<br />

4.4<br />

3.8<br />

3.6<br />

3.4<br />

3.2<br />

3.0<br />

2.8<br />

material and pressure diffusion. Simulations were<br />

2.6<br />

conducted to evaluate the stress in the particle and in the<br />

2.4<br />

binder during delithiation to understand the cause <strong>of</strong><br />

failure <strong>of</strong> the battery electrode.<br />

Results<br />

Transport studies on NMC cathodes. The change <strong>of</strong><br />

electrode potential during passage <strong>of</strong> current provides an<br />

overview <strong>of</strong> the electrode behavior, such as electrode<br />

capacity and rate, and cycle performances. Figure V - 197<br />

shows the charge and discharge curves on a thin NMC<br />

electrode measured at various rates. The charge and<br />

discharge curves were obtained in separate experiments<br />

and plotted together to compare the differences. The<br />

electrode capacity measured at the end <strong>of</strong> charge/discharge<br />

at C/25 is ca. 160 mAh/g. More than 50% <strong>of</strong> the capacity<br />

was still retained when discharged at rates up to 100C.<br />

This capacity retention observed on the thin NMC<br />

electrodes is much higher than that reported on the thicker<br />

electrodes made <strong>of</strong> the same material. An even higher rate<br />

capability was seen for charge cycles and a clear<br />

asymmetry between the charge and discharge was<br />

observed.<br />

The high rate capability <strong>of</strong> the NMC electrode was<br />

explored by examining the transport properties <strong>of</strong> the<br />

material at the particle scale. Since the electrodes were made<br />

to have approximately one to two layers <strong>of</strong> NMC particles on<br />

the current collector, porous electrode effects are minimized.<br />

The NMC particle is assumed to be a nonporous sphere<br />

and to be representative <strong>of</strong> the whole electrode. The<br />

diffusion <strong>of</strong> Li inside the NMC particle is assumed to be<br />

the limiting process <strong>of</strong> the intercalation reaction and is<br />

described by Fick’s second law. Figure V - 198 shows the<br />

estimated Li diffusion coefficients at various states <strong>of</strong><br />

charge. The diffusion coefficient is strongly dependent on<br />

Li concentration. The increasing diffusion coefficient with<br />

100C<br />

100C<br />

Thickness = 6m<br />

Loading = 0.49 mg/cm 2<br />

50C<br />

10C<br />

1C<br />

C/25<br />

C/25<br />

1C<br />

10C<br />

50C<br />

0 20 40 60 80 100 120 140 160 180<br />

Capacity (mAh/g)<br />

Figure V - 197: Experimental charge and discharge curves on a NMC thin<br />

electrode (~6 µm) at various rates. The charge and discharge curves,<br />

obtained in separate experiments, are plotted together to compare the<br />

differences.<br />

D (m 2 /sec)<br />

Li<br />

1E-13<br />

1E-14<br />

1E-15<br />

1E-16<br />

Discharge<br />

Charge<br />

0.0 0.2 0.4 0.6 0.8 1.0<br />

SOC<br />

Figure V - 198: Estimated lithium diffusion coefficient as a function <strong>of</strong> state<br />

<strong>of</strong> charge (SOC). The charge data (•) was obtained by charging the<br />

electrode with several current interruptions, and the discharge data () was<br />

obtained by discharging the electrode with several current interruptions to<br />

estimate the diffusion coefficients at various SOC.<br />

Particle size study on LiFePO 4 cathodes. During<br />

discharge, the smaller particles lithiate at a higher rate than<br />

the larger particles. The self-regulating mechanism does<br />

not exist in the flat-potential system, and therefore there is<br />

a disparity in the level <strong>of</strong> lithiation between the small and<br />

large particles. During charge, on the other hand, the<br />

smaller particles delithiate at a higher rate and have<br />

smaller Li content. The path dependency on the amount <strong>of</strong><br />

Energy Storage R &D 642 FY 2011 Annual Progress Report

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