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