Whatever way we cool a battery cell we will create temperature gradients in the cell.
It is not possible to apply cooling to all of the active area of the electrodes, this would be nice, but would significantly reduce the energy density of the overall battery pack. So we have to apply cooling to the outside surface of the cell.
Let’s start with the basics and look at thermal conduction.
We have a material of length, d and cross-sectional area, A that is hot, T2 at one end and cold, T1 at the other end. Knowing the thermal conductivity, k of the material we can calculate the heat, Q.
The maximum working temperature difference end to end is normally specified by the cell manufacturer as 2°C.
A 2°C temperature gradient would be generated with a heat flux of 0.11W. If the cell has an internal resistance of 0.025Ω then a current of 2.14A would generate a joule heating value of 0.11W, this is a discharge rate of less than 0.5C, this cell is not being pushed hard.
This temperature difference might be allowed to increase to 5°C or even 10°C for short transient events.
We could increase the area of contact between the coolant and the cell, this would give a greater heat flux for a given temperature delta.
- radial thermal conductivity = 0.83 W/m.K
- distance d = 0.021m
- cross-sectional area, A = 0.00108 m2
Note: I’ve tried to align the assumptions on this calculation with the bottom cooled cell and used the same equations. This means I have assumed a contact area of 18mm x 60mm and assumed this is a rectangular block of active material. Perhaps some big assumptions, but this is a rough estimate. A 2°C temperature gradient would be generated with a heat flux of 0.09W and shows that these two methods are roughly comparable.
This is very approximate as the joule heating is distributed throughout the cell, however, this gives a feel as to the steady state conditions under which a temperature gradient can be generated.
If you have run full 3D thermal calculations on cell cooling systems that you can share online then do please drop us a line.
- Guilherme Matheus Todys, S M Shadhin Mahmud, “Thermal Characterization of a Cylindrical Li-ion Battery Cell“, Masters Thesis, Chalmers University of Technology
- Yannic Troxler, Billy Wu, Monica Marinescu, Vladimir Yufit, Yatish Patel, Andrew J. Marquis, Nigel P. Brandon, Gregory J.Offer, “The effect of thermal gradients on the performance of lithium-ion batteries“, Journal of Power Sources, Volume 247, 1 February 2014, Pages 1018-1025
There are a number of battery cooling options and all of them create this temperature gradient to a greater or lesser extent.
We can blow air over the cells or run a cooling plate next to the cells. The larger the difference in temperature between the cell surface and the cell core the higher the heat flux, but also the higher the temperature gradient.
The dielectric cooling system immerses the cells in the fluid, thus maximising the surface contact area and giving the highest possible heat flux. However, this comes at the expense of weight and complexity.
If you want to extend the lifetime of the cell you need to reduce the temperature of the cell. However, you need to ensure that you don’t create such a high temperature gradient that the cell ages rapidly in some areas. This creates a conflict that has to be taken into account in the design of the cooling system and the control strategy for the cooling system.
Heat generation in a cell can be defined quite simply for the case where the cell is operating within it’s normal limits. The first expression gives the heat flow [W].
The first part of this equation is the irreversible Joule heating term, the I2R term.
The second part is the reversible entropy term or Reaction heat terms. The charge and discharge reaction can be exothermic or endothermic under certain conditions.
This changes depending on whether you are looking in plane or through plane. In-plane the conductivity will be dominated by the metallic electrodes and is approximately 10x to 100x greater than the through plane conductivity.