Implementation of Battery Digital Twin: Approach, Functionalities and Benefits
Abstract
:1. Introduction
- Limited use cases and implementation results available to learn from others;
- No clear guidance on how much to budget;
- Difficult to know where to start to get value quickly;
- Initiatives that are misleadingly branded as “Digital Twin”;
- Limited know-how.
2. Battery DT Functionalities during Operation and End-of-Life
- Some articles only mentioned battery DTs as a possible application
- Some of them did not explain the architecture to support battery DTs
- Others were only theoretical articles.
- Battery DT influence on life cycle phases;
- Current BMS functionalities.
3. Approach
3.1. Step 1: Lightweight or Heavyweight Battery Model Development
- Electrical model (ECM);
- Electrochemical model (P2D);
- Thermal model;
- Mechanical model;
- Interdisciplinary combined model.
- Battery dynamics represented by the model
- Number of parameters
- Computation time
- Accuracy
- Ease of understanding and complexity for implementation.
Experimental Parameter Identification Techniques
3.2. Step 2: Impact Analysis of Real-World Charge/Discharge Cycles on Battery Model Parameter
3.3. Step 3: Model Parameter-Update Estimation
- Calculate the model parameters at the end of N cycles, and repeat the update process iteratively. Identify the reduced set of parameters (such as in Table 1) directly influenced by the number of cycles and operating conditions. The initial conditions (from the governing equations) of the model are certainly updated. Thus, new parameters set and initial conditions are available to the model for its next simulation (N cycles). For DFN, the mathematical estimations of parameters mainly involves revaluating the governing equations which employs Fick’s law of diffusion, charge and mass conservation, concentrated solution theory and Butler-Volmer electrochemical kinetic expression.
- Calculate the rate of degradation physics caused by lithium plating and SEI growth through the reaction equations and rate expressions [62]. Lithium-plating passive film layers formed by consuming of cyclable Li-ions is influenced by the charge transfer mechanism. The rate of SEI formation reaction is affected by mass transport within the anode and by surface kinetics. Effects of degradation physics are integrated in the model after every N cycles.
- Utilize the fast minimization algorithms such as Gauss-Newton method, prediction error minimization by estimating the parameter-update through synthetic experimental data [63]. Synthetic experimental data can be obtained using simulated battery output with computer-generated randomness. However, this method has an unjustified validation scheme because the input would also be simulated; hence this approach is mainly beneficial for initial testing purposes of the battery DT.
- Apply data-driven parameter identification methods estimation which employs the terminal voltage and load current for parameter update (partially applied in [64]). A comprehensive literature survey of the data-driven parameter identification methods is not conducted. Therefore, this paper does not attempt to review the data-driven parameter identification methods thoroughly. Instead, we choose to review if data-driven approaches can support the parameter-update step. There is no doubt that a large amount of training data (collected at the beginning of life) is a requirement for data-driven parameter-update during usage. Nonetheless, the cost and computation time of the data-driven algorithms [65,66] for application in battery DT need to be compared.
3.4. Step 4: Adaptive Model Update
3.5. Step 5: Battery DT KPI Quantification
- Investment
- ◦
- Effect on optimization cost due to battery DT functionalities.
- ◦
- Cost to establish data acquisition from BMS to the battery model. Here, we assume the preexisting cost of sensors installed on the BMS and the cells.
- ◦
- Cost of data storage method, i.e., cloud server, memory drive, etc.
- ◦
- Computational cost of simulating the algorithms of the battery DT.
- Time
- ◦
- Time needed for the state estimation algorithms, optimization algorithms and other battery DT functionalities
- ◦
- Time to retrieve battery data from its application and assign it to the DT
- ◦
- Speed of battery DT alignment with actual battery, i.e., total time for executing the parameter-update step.
- Accuracy
- ◦
- Accuracy of parameter identification.
- ◦
- Accuracy of parameter-update estimation parameter identification.
- ◦
- Accuracy of state estimation
- Functionalities
- ◦
- DT functionalities that support the battery designers (battery design optimization)
- ◦
- DT functionalities that support the battery users
- ◦
- DT functionalities that support the battery EoL handler (RUL assessment)
4. Results
5. Discussion
- Level of fidelity expected from a battery DT—A model that captures the electrical, thermal, electrochemical, mechanical and aging aspects of a battery is deemed a high fidelity model. The reality and practicality of such a model are not clear. The cost and time needed for an exhaustive high-fidelity battery DT are high, and the estimate of accuracy improvement is also missing;
- Number of DTs across the battery lifecycle—The idea of a DT across the lifecycle of a product is not entirely understood. This is due to the uncertainty of the number of DTs needed in such cases. Either there is one DT with a large capacity, or there are many small-sized DTs coupled together. For battery DT, the coupling of process and product DT is a possible use case during manufacturing;
- Scaling the battery DT to module and pack-level DT—Achieving battery DTs at scale will require a reduction in technical barriers for their adoption. This implies that for a pack-level battery DT, the number of sensors and the amount of data retrieved will drastically increase. Hence, the data acquisition and storage needs to be seamless;
- Accuracy of behavioral prediction using battery DT—For commercial utilization of battery DTs, it is necessary to compare and quantify the accuracy of existing BMS predictions vs. the prediction of battery DT. Quantification and comparison of percentage error in DT estimations should be the primary focus in future works.
6. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
Appendix A
DFN Model | Derived through | Governing Equations 1 |
---|---|---|
Solid phase mass transport equation—Li+ concentration in electrodes and separator | Fick’s law of diffusion | |
Liquid phase mass transport equation—Li+ concentration in electrolyte | Conservation of Li+ ions (Conservation of mass) | |
Solid phase charge transport equation—Potential in electrode | Ohm’s law (Conservation of charge) | |
Liquid phase charge transport equation—Potential in electrolyte | Ohm’s law and Kirchhoff’s law (Concentrated solution theory, conservation of charge) | |
Flux density between solid and liquid phase | Butler-Volmer Equation |
ECM Model Equations | Variables |
---|---|
pi = fi(SOC, SOH, T, I) p1 = {VOCV, R1, C1, RS} | i is the i-th parameter of the model. R1 and C1 are the polarization resistance and capacitance and RS is the ohmic resistance. VOCV is the open circuit voltage |
Vt = VOCV − V1 − VRs; VRs = I * RS | where VRs refers to the voltage reduction from Rs and Vt is the terminal voltage |
SOC = SOC0 − | SOC calculation using CC, where C is capacity, Ib is current, and SOC0 is the initial SOC |
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Reference | Implementation Method 1 | DT Functionality |
---|---|---|
[21] | HI and LSTM algorithm | Estimation of battery’s actual discharge capacity |
[22] | Cloud BMS with AEHF-based SOC estimation algorithm and PSO-based SOH estimation algorithm | Estimation of SOC, SOH, capacity fade, power fade |
[23] | On-board diagnosis to cloud environment; ECM model parameter fitting, curve fitting and SOC-OCV curve | SOC, capacity, internal resistance, SOH-R, SOH-C |
[24] | Visual software in LabVIEW; ECM with SVM and filter algorithms | DT platform for spacecraft lithium-ion battery pack degradation assessment; SOC estimation |
[25] | Cloud connected BMS; electric-thermal model and empirical ageing model | Cell voltage and temperature |
[26] | ECM and EFK algorithm | SOC estimation |
[27] | Review paper on battery DT | Battery DT framework and its cyber-physical elements |
[28] | Offline—Regression model using sparse-Proper Generalized Decomposition (s-PGD); Online—Dynamic Mode Decomposition technique | Cell voltage, anode/cathode bulk SOC, anode/cathode surface SOC |
[29] | Linking reduced order model with ECM in Ansys Twin Builder | Real-time temperature of the battery pack at different locations; What-if scenarios for root cause analysis |
Parameters | Symbol (Unit) 1 | High Cycle Number | High C-Rate |
---|---|---|---|
DFN | |||
Thickness | Lp, Ln, Ls (µm) | x [55] | Moderate [55] |
Surface area | Ap, An, As, (m2) | x [48] | Moderate [55] |
Particle radius | Rp+, Rp− (µm) | x [54] | x [54] |
Active/Inactive material volume fraction | εsp, εsn | x [55] | Moderate [55] |
Electrolyte phase volume fraction | εep; εen | - | - |
Maximum Li+ concentration | csp,n,se (mol cm−3) | x [48] | Moderate [55] |
Average electrolyte concentration | ce (mol cm−3) | - | x [48] |
Stoichiometry of n, p at 0% and 100% SOC | xp,n0,100 | - | - |
Diffusion coefficient in solid and liquid phase | Dsp, Dsn, De (m2 s−1) | x [54] | - |
Solid phase conductivity | σsp, σsn (µm) | x [48] | x [48] |
Li transference number | t+0 | Not sensitive [54] | Not sensitive [54] |
Resistivity of film layers (including SEI) | Rf (Ω) | Not significant [54] | x [48] |
Negative electrode potential, U− coefficients | - | x [48] | - |
Positive electrode potential, U+, coefficients | - | x [48] | - |
Open circuit potential | V | x [48] | - |
Overpotential | η | Not significant [55] | - |
Reaction flux at the solid particle surface | j (mol cm−1 s−1) | - | - |
Exchange (electrolyte and solid) current density | ie (A cm−2) | - | - |
Electrolyte activity coefficient | ±f | C | C |
Bruggeman porosity exponent | p | C | C |
Anodic/Cathodic charge transfer coefficient | αa, αc | C | C |
Intercalation/deintercalation reaction-rate coefficient | kn,p (A cm2.5 mol−1.5) | C | C |
Universal gas constant | R | C | C |
Absolute temperature | T | C | C |
Faraday’s constant | F | C | C |
ECM | |||
Internal ohmic resistance | RO (Ω) | Sensitive [56] | Sensitive [56] |
OCV | VOCV (V) | ||
Polarization Resistances | R1, R2… (Ω) | ||
Polarization Capacitances | C1, C2… (F) | ||
Coulomb efficiency | η | Almost constant [57] | Sensitive [57] |
Hysteresis voltage, hysteresis decaying factor | H (V), k | Not significant [58] | Impact of overvoltage [59] |
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Singh, S.; Weeber, M.; Birke, K.P. Implementation of Battery Digital Twin: Approach, Functionalities and Benefits. Batteries 2021, 7, 78. https://doi.org/10.3390/batteries7040078
Singh S, Weeber M, Birke KP. Implementation of Battery Digital Twin: Approach, Functionalities and Benefits. Batteries. 2021; 7(4):78. https://doi.org/10.3390/batteries7040078
Chicago/Turabian StyleSingh, Soumya, Max Weeber, and Kai Peter Birke. 2021. "Implementation of Battery Digital Twin: Approach, Functionalities and Benefits" Batteries 7, no. 4: 78. https://doi.org/10.3390/batteries7040078
APA StyleSingh, S., Weeber, M., & Birke, K. P. (2021). Implementation of Battery Digital Twin: Approach, Functionalities and Benefits. Batteries, 7(4), 78. https://doi.org/10.3390/batteries7040078