From Butler-Volmer equation, exchange current density jo can be utilized to evaluate the kinetics at solid/electrolyte interface. Thus, we applied two methods - electrochemical impedance spectroscopy (EIS) and potentiostatic intermittent titration technique (PITT) to study the exchange current density of NCA at different SOC using the same dense bulk pellets2. Primary results of these measurements are shown in Fig. 1. Exchange current density from PITT is found to decrease with increasing SOC, whose value is nearly 102smaller at high SOC (70 %) than that of pristine NCA. However, EIS results show discrepancy above 50 % SOC.
Based on the PITT results from bulk pellets, relative contributions of bulk and interfacial transport of the particles can be modeled using Biot numbers Λ and time constant analysis. Fixing the acceptable overpotential as 0.1 V, the rate of bulk diffusion and interfacial reaction of the 5.6 um commercial spherical NCA particles are plotted as Fig. 2. With increasing SOC, the maximum C-rate decreases by almost 102 and Λ is of order 100 indicating the mixed-control kinetics. In other words, the interfacial reaction clearly becomes the rate-limiting kinetic step and thus determine the rate-performance of NCA.
This work was supported as part of the North East Center for Chemical Energy Storage (NECCES), an Energy Frontier Research Center funded by the U.S. Department of Energy, Office of Science, Basic Energy Sciences under Award # DE-SC0012583.
References:
[1]. R. Amin, D.B. Ravnsbaek, Y.-M. Chiang, J. Electrochem. Soc. 2015, 162, A1163-A1169.
[2]. J. Li, X. Xiao, F. Yang, M. W. Verbrugge, Y.-T. Cheng, J. Phys. Chem. C. 2012, 116, 1472–1478.