Analysis of Charge-Discharge Rate Influences LCO/Graphite Pouch Cell Volume Expansion During Rest Periods

Table of Contents

1. Preface

Lithium-ion batteries undergo volume expansion during formation, cycling, storage, and overcharge, stemming from both structural changes and gas evolution. The charge discharge rate determines the speed of lithium (de)intercalation and is accompanied by varying degrees of heat generation or lithium plating. Researchers often include a rest period after charge or discharge to allow the cell to stabilize, mitigating thermal and polarization effects. But how does cell volume behave during this rest phase?

This study investigates the impact of C-rate by in-situ monitoring the volume expansion of Lithium Cobalt Oxide(LCO)/Graphite pouch cells during rest after different charge discharge rate cycles.

Figure 1. Various factors affecting the fast charging of lithium-ion batteries

Figure 1. Various factors affecting the fast charging of lithium-ion batteries[1]

2. Experimental Setup

2.1 Test Equipment

The In-situ Gassing Volume Monitor GVM2200 from IEST was used (Figure 1). This instrument allows precise temperature control from 20°C to 80°C and real-time monitoring of cell volume changes.

In-Situ Battery Gassing Volume Analyzer (GVM2200)

Figure 2. In-Situ Battery Gassing Volume Analyzer (GVM2200)

2.2 Cell Information & Test Parameters

The test cell specifications are listed in Table 1. Four experimental groups with different charge-discharge protocols were defined (Table 2). Each cycle concluded with a one-hour rest period. The cells were then placed in the GVM2200 with the oil bath set to 25°C for continuous volume monitoring.

Table 1. Cell Information

Table 1. Cell Information

Table 2. Charge and Discharge Parameters

Charge and Discharge Parameters

Note: *Four distinct protocols were tested, varying the constant current (CC) charge rate, the inclusion of a constant voltage (CV) phase, and the discharge rate. All protocols included a 1-hour rest after both charge and discharge.*

3. Results & Analysis

3.1 In-situ Monitoring of Full-Cycle Volume Expansion

The voltage and volume expansion curves for the four cycles are shown in Figure 3. During the CC charge phase, volume increased steadily with rising State of Charge (SOC), primarily due to graphite intercalation. Upon entering the CV and subsequent rest phase, the cell volume began to contract, gradually stabilizing.

During the CC discharge phase, volume contracted as Depth of Discharge (DOD) increased. A notable initial anomalous expansion was observed at the start of discharge, which diminished as the discharge rate decreased. Volume continued to decrease during the post-discharge rest before stabilizing.

Figure 3. Cell voltage and volume change curves under different charge-discharge currents.

Figure 3. Cell voltage and volume change curves under different charge-discharge currents.

3.2 Analysis of Volume Change During Post-Charge Rest

Zooming into the post-charge rest periods (Area ‘A’ in Figure 3) reveals a key trend, as detailed in Figure 4. The first cycle, which lacked a CV phase and ended with a 1C charge rate cutoff, showed significant volume contraction during the 1-hour rest, taking approximately 1500 seconds to stabilize.

In contrast, cycles 2-4 included a CV phase, reducing the cutoff current to below 0.1C. For these cycles, the volume contraction primarily occurred during the CV phase itself. The subsequent rest period showed minimal further volume change. This indicates that volume relaxation is closely tied to current reduction and internal polarization. A CV phase effectively reduces polarization and lithium concentration gradients before the rest period begins, minimizing subsequent relaxation. Without a CV phase, the high internal polarization at the end of a CC charge requires a substantial rest period (≥30 minutes) for stress and strain to release and reach a steady state.

Figure 4. The effect of charge cutoff current on volume change during rest

Figure 4. The effect of charge cutoff current on volume change during rest

3.3 Mechanistic Insights from Electrochemical-Mechanical Modeling

In order to further explain the process of lithium-ion transmission and charge state evolution in the constant current-constant pressure charge process, the mechanical-electrochemical model is used to study the distribution of lithium concentration, stress and strain in the charging process.

During the constant flow charging phase, lithium-ion are continuously embedded in the graphite layer, which leads to structural swelling. As the SOC continuously grows, the volume constantly expands. When the constant current charging is completed, the lithium ion concentration in the electrolyte, the lithium concentration in the negative electrode particles, the strain, and the stress are as shown in Figure 5. Figure 5 (a) shows that the closer the cathode fluid collection is, the higher the lithium-ion concentration in the electrolyte is. This is because the positive / negative particles near the diaphragm are preferentially lithium / lithium. At the end of constant current charging, the degree of lithium removal / lithium removal of the particles near the diaphragm is greater than that of the particles near the fluid collection. From Figure 5 (b), higher lithium concentration in the negative particles close to the diaphragm. This is because the electrolyte in the negative region away from the diaphragm has a longer lithium diffusion distance than the negative particles near the diaphragm, allowing the lithium-ion reaching the anode to be preferentially inserted into the particles close to the diaphragm.

In the negative electrode particles near the diaphragm, the solid-phase lithium concentration is higher, so their strain is also higher, as shown in Figure 5 (c). Meanwhile, the strain is greater on the free surface of the particles, but less so on the contact surface between the particles and between the particles and the boundary. This is because the insertion of lithium ions causes the volume swelling of the particles. The free surface of the particles expands outward, leading in greater deformation. However, the deformation on the contact surface is smaller under the constraints of adjacent particles and boundaries. Figure 5 (d) shows that the stress distribution is opposite to the strain distribution. This is because the free surface of the particles is unconstrained and therefore stress less. However, the contact surface is strongly constrained and therefore greater stress. The maximum stress is located in the particles close to the diaphragm. The average strain of the negative electrode particle (meaning the mean value of the whole body of the particle in the electrode) during the constant current charging is shown in Figure 6. Both increase gradually with time, and their change trend is basically consistent with the relationship shown in Figure 3. After CC charging, the average strain and average stress reach the maximum value respectively.

Figure 5. Lithium-ion concentration (a) and graphite particle solid phase lithium concentration (b), strain (c) and stress (d) distribution of graphite particles at the end of 1C CC charging

Figure 5. Simulated distributions at the end of 1C CC charging: (a) Li+ concentration in electrolyte, (b) solid-phase Li concentration in graphite, (c) strain in graphite particles, (d) stress in graphite particles [2]

Figure 6. Average strain and average stress of the anode particles during charging

Figure 6. Average strain and average stress of the anode particles during charging[2]

3.4 Analysis of Volume Change During Post-Discharge Rest

The volume behavior during post-discharge rest (Area ‘B’ in Figure 3) is shown in Figure 7. A clear correlation exists: as the discharge rate decreases, both the magnitude of volume change during rest and the time required to stabilize also decrease.

This phenomenon mirrors the post-charge behavior and is similarly linked to internal polarization and inhomogeneous lithium concentration profiles established during discharge. Simulations confirm that higher discharge rates or thicker electrodes lead to greater lithium concentration gradients at the end of discharge (Figure 8), resulting in larger stress/strain gradients that relax during rest, causing measurable volume contraction.

Furthermore, the anomalous initial expansion observed at the start of discharge (Figure 3) becomes less pronounced at lower discharge rates. This suggests this expansion may also be related to thermal effects induced by high currents.

Figure 7. The effect of discharge current on volume change during the subsequent rest period.

Figure 7. The effect of discharge current on volume change during the subsequent rest period.

Figure 8. Discharge current effect on total volume and bounce volume

Figure 8. Discharge current effect on total volume and bounce volume

Similar to the simulation results of the constant current-constant voltage (CC-CV) charging process, during constant current (CC) discharging, lithium deintercalates from the negative electrode particles while simultaneously intercalating into the positive electrode particles as the discharge proceeds. Concurrently, the electrochemical potential drives the migration of lithium ions in the electrolyte from the negative electrode to the positive electrode. The lithium concentration within the negative electrode particles decreases, whereas it increases within the positive electrode particles.

Similarly, along the electrode thickness direction, an inhomogeneous distribution of lithium concentration exists. The magnitude of this concentration gradient is related to both the electrode thickness and the discharge rate. As shown in Figure 11, at the end of discharge, the lithium concentration distribution is relatively uniform when the electrode is thin or the discharge rate is low. However, pronounced concentration gradients emerge with increased electrode thickness or higher discharge rates. Specifically for the positive electrode, particles near the separator exhibit a higher lithium concentration compared to those near the current collector.

Consequently, as the discharge rate decreases, the internal lithium concentration gradient within the cell diminishes. This leads to a reduction in the stress and strain induced by concentration differences. As a result, the magnitude of volume change during the subsequent rest period becomes smaller, and the time required for the volume to stabilize is shortened.

Figure 9. Distribution of lithium concentration in the solid phase of the particles at the end of discharge

Figure 9. Distribution of lithium concentration in the solid phase of the particles at the end of discharge[3]

4. Summary

This study utilized the in-situ GVM2200 system to monitor the volume expansion behavior of Lithium Cobalt Oxide(LCO)/Graphite cells at different charge discharge rates. The findings reveal that volume changes during cycling and rest are influenced not only by lithium (de)intercalation but also by internal polarization, inhomogeneous lithium distribution, and associated thermal effects.

A key practical insight is that implementing a CV charge phase with a low cutoff current (e.g., <0.1C) can effectively homogenize the cell’s internal state before rest, minimizing post-charge volume relaxation. Conversely, since discharge often occurs at higher rates, a sufficient rest period should be allocated post-discharge to allow the cell to reach a stable state before subsequent testing or characterization.

5. References

[1] Anna Tomaszewska, Zhengyu Chu, Xuning Feng, et al.Lithium-ion battery fast charging: A review,eTransportation, 1 (2019) 100011.

[2] Factors affecting stress in anode particles during charging process of lithium ion battery, Journal of Energy Storage, 43(2021)103214.

[3] Hideki Kikukawa, Kohei Honkura, Michihisa Koyama.Influence of inter-particle resistance between active materials on the discharge characteristics of the positive electrode of lithium ion batteries, Electrochimica Acta, 278(2018)385-395.

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