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CATL NMC811 vs LFP Batteries: Thermal Runaway Comparison

NMC811
NMC811
CATL NMC811 vs LFP Batteries: Thermal Runaway Comparison
CATL NMC811 vs LFP Batteries: Thermal Runaway Comparison

 

This paper presents a comparative study on the thermal runaway propagation of CATL batteries using NMC811 and LFP as cathode materials. The main conclusions are as follows:

Thermal Runaway Propagation Characteristics

The peak temperature during thermal runaway of NMC811 batteries (899°C) is significantly higher than that of LFP batteries (524°C). In addition, the thermal runaway propagation speed of NMC811 batteries is five times that of LFP batteries. This indicates that NMC811 batteries require additional safety measures, such as inter-cell spacing and thermal barriers, to meet safety standards.

Gas Emission

The gas volume, gas flow rate, and gas temperature released by NMC811 batteries during thermal runaway are all higher than those of LFP batteries. This requires the use of ventilation channels or high-temperature-resistant potting materials in NMC811 battery modules to isolate vented gases and avoid increased heat input, abrasion, and arcing risks.

Battery Damage

NMC811 modules exhibit higher risks of damage severity, material ejection, and side-wall rupture than LFP modules. Therefore, structurally reinforced potting materials or high-temperature-resistant materials (such as steel battery casings) are recommended to maintain the mechanical integrity of NMC811 batteries and ensure unobstructed vent gas discharge.

Due to their high nickel content, NMC811 batteries feature higher energy density. As shown in Figure 1, compared with LFP batteries, NMC811 batteries provide 32% higher gravimetric energy density and 37% higher volumetric energy density. In terms of safety, LFP batteries perform excellently and are less prone to overheating, combustion, and other hazardous conditions, benefiting from the stability and thermal resistance of their cathode materials.

To compare their thermal runaway propagation processes, CATL NMC811 and LFP batteries were selected for this study. Detailed specifications are listed in Table 1:

  • NMC811 battery: 213 Wh/kg, 549 Wh/L, 96 Ah
  • LFP battery: 164 Wh/kg, 373 Wh/L, 160 Ah

 

Energy Density Comparison: NMC vs LFP Batteries
Energy Density Comparison: NMC vs LFP Batteries

 

Table 1
Table 1

 

As shown in Figure 2, five batteries were assembled into a small module. A heating plate was installed on one side of the module to trigger thermal runaway by heating one of the batteries, with a heating power of 6.2 W/cm².

Thermocouples were placed between the batteries, on the battery surfaces, and near the safety valves to monitor temperature. The final experimental setup is shown in Figure 3, and a camera was used to record the thermal runaway process.

For accurate thermal runaway testing and precise temperature monitoring, Neware Battery Testing Systems paired with Neware Thermocouple Aux Channels are highly recommended.

 

Figure 2 Schematic Diagram of the Small Battery Module
Figure 2 Schematic Diagram of the Small Battery Module

 

Figure 3 Experimental Setup for Battery Thermal Runaway
Figure 3 Experimental Setup for Battery Thermal Runaway

 

Figure 4 shows the measured data of thermal runaway propagation in batteries, mainly including temperature and voltage. Blue and green represent internal temperatures between cells, while gray represents the surface temperature of the module.

The start time of the heating plate heating stage is set as . The onset of thermal runaway propagation is defined as the point when heating ends and temperature rises abruptly. The NMC811 module reached this point at a surface temperature of 371.6 °C. In contrast, thermal runaway in the LFP battery occurred much later, at 436.6 °C.

Due to unilateral heating, a temperature gradient was generated across the cells. For the NMC811 module, the front temperature was 371.6 °C and the rear temperature was 33.9 °C; thermal runaway initiated as the energy balance between internal heat generation and dissipation within the cell was disrupted. The LFP battery entered thermal runaway at a front temperature of 436.6 °C and a rear temperature of 41.6 °C.
The average peak temperature of the NMC811 battery was 899.3 °C, significantly higher than the 524.4 °C of the LFP battery.
Figure 4 Measured data of thermal runaway propagation: Blue/green indicates inter-cell temperature, gray indicates surface temperature; (a) NMC811, (c) LFP. Cell voltage: (b) NMC811, (d) LFP.
Figure 4 Measured data of thermal runaway propagation: Blue/green indicates inter-cell temperature, gray indicates surface temperature; (a) NMC811, (c) LFP. Cell voltage: (b) NMC811, (d) LFP.

 

As shown in Figure 5, thermal runaway of a single cell (Cell 2 in Figure 5) within the battery module can be divided into three stages:

Stage 1: Heating caused by thermal runaway of the adjacent Cell 1;

Stage 2: Thermal runaway triggered in the first jellyroll of Cell 2;

Stage 3: Internal thermal runaway propagates to the second jellyroll in Cell 2.

 

Figure 5 Three Stages of Thermal Runaway in Cell 2
Figure 5 Three Stages of Thermal Runaway in Cell 2

 

The exact onset time of battery thermal runaway is determined by the following two criteria:

(1) The battery voltage begins to drop, i.e., the voltage change becomes negative;

(2) The temperature rise rate of any temperature sensor on the battery surface exceeds 10 K/s.

Based on the data shown in Figure 4 and the propagation mechanism illustrated in Figure 5, the time interval of thermal runaway between batteries can be further subdivided into the thermal runaway reaction time ΔtTR and the pause time ΔtP,TR. During the pause period, heat transfer to adjacent batteries mainly occurs.

For thermal imager and video data, the thermal runaway time is evaluated according to the visible time span of gas venting from the safety valve.

 

Figure 6 shows the time interval between thermal runaway events and their components for the two types of batteries.

For LFP batteries, the time interval between thermal runaway events is distributed around an average value of 460 seconds, and the thermal runaway reaction time is distributed around an average value of 254.2 s.

For NMC811 batteries, the time interval between thermal runaway events increases exponentially, and the thermal runaway reaction time of NMC811 batteries is distributed around an average value of 17.4 s.

Figure 6 Thermal Runaway Time
Figure 6 Thermal Runaway Time
Analysis of thermally runaway batteries shows that the mass loss of NMC811 batteries ranges from 39.6% to 48.7%, which reduces their mechanical integrity and the clamping force between cells, resulting in higher thermal contact resistance and slower thermal propagation. In contrast, LFP batteries maintain their mechanical integrity with significantly lower mass loss, ranging from 20.9% to 21.6%.
From the images of the NMC‑811 battery module after testing, significant deformation of the cell casing and damage to the cell cover can be observed. Combined with 45.8% material ejection, this resulted in the loss of mechanical integrity.
Although initial venting occurred through the safety valve, sidewall rupture also took place due to temperatures exceeding the melting point of the aluminum cell casing. In contrast, LFP batteries released gas only through the safety valve, with no obvious sidewall rupture.
Figure 7 Batteries After Testing
Figure 7 Batteries After Testing

 

For more details, please refer to the reference:

Schöberl, J., Ank, M., Schreiber, M., Wassiliadis, N., & Lienkamp, M. (2024).

Thermal runaway propagation in automotive lithium-ion batteries with NMC-811 and LFP cathodes: Safety requirements and impact on system integration.

*eTransportation*, 19, 100305.

https://doi.org/10.14459/2023mp1717758