Introduction
Reconfigurable battery packs have the advantage of altering the pack topology to adapt to changes in load requirements. The series/parallel battery configuration allows a low cost solution for networks under constraint to meet the energy and power demand placed on an electrical system without adding additional batteries and incurring additional cost. Part of the system is dependent on the fast charging parallel converter which allows the network to balance each cell and accurately estimate the battery SOC. Kim, Qiao, and Qu[1] series cell array negated parallel configurations in their series cell arrays. Physical based models have the advantage of performing comprehensive analysis on the effects of both the solid phase and the liquid phase. Modelling, porous electrode theory coupled with transport phenomena and electrochemical reactions represented by coupled nonlinear partial differential equations (PDE) in one or two dimensions gives physical based models an advantage over equivalent circuit model (ECM) based models. Santhanagopalan[2] and Rahimian[3] have used the single-particle model (SPM) implementing Kalman filtering methods to estimate SOC of Li-Ion cells. An area of concern is the computational complexity of the physical based models.
Fig-1
Experimental Method
State of Charge (SOC)
The SOC, a measure of remaining capacity in the battery, helps to ensure during charging battery cells are not over/under charged and during discharge it is a quick gauge to show how much capacity is remaining capable of supporting the load.
Eq-1
where, Q is the capacity. In battery cells, capacity can be represented as a voltage at specific time.
Fig-2
State of Health (SOH)
The SOH, an indication of where the battery is at in its life cycle, is used to measure capacitance of the used battery relative to the capacitance of a new battery. Using capacity fade analysis to demonstrate the loss of capacity during the life of the cell indicates if the battery is being maximized. This allowed us to monitor the remaining capacitance available in the battery cell at a given time.
Eq-2
where, c is the capacity, α is the deterioration rate multiplier. α varies depending on power density, energy density, and temperature components.
Fig-3
Fig 3a shows that as the discharge rate increases the capacitance decreases. Fig 3b indicates that colder temperatures have an adverse effect on the current and at 0o F some capacitance is lost during the electrochemical process. Fig 3b shows that there are little losses from 60o – 100o F.
Remaining Useful Life (RUL)
The RUL, an approximation of the cyclability of a battery pack, enables an estimation of the number of duration individual battery cells within the series/parallel battery scheme are useable, thus approximating the life cycle of the entire BMS.
Eq-3
where, β is the cycle deterioration factor.
Fig-4
Fig 4 illustrates that singular variables introduced into the process could have minor effects on the overall battery cell if monitored by the BMS. The introductions of multiple factors at the same time could have extreme effects on the BMS system.
Ref
- Kim, T., et al. “Series-Connected Self-Reconfigurable Multicell Battery.” 26th AAPEC&E, Mar. 2011, IEEE. pp. 1382-1387.
- Santhanagopalan, S., et al. "Review of Models for Predicting the Cycling Performance of Lithium Ion Batteries." JPS 156.2 (2006): 620-628.
- Rahimian, S.K., et al. “State of Charge and Loss of Active Material Estimation of a Lithium Ion Cell under Low Earth Orbit Condition Using Kalman Filtering Approaches.” JES (2014): A860-A872.