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These poorly soluble and highly insulating species are produced at the end of discharge, and are responsible for the positive electrode passivation and the early end of discharge.
However, a reversible broadening of the XRD peak was observed at the end of discharge, indicating some structural changes.
As the end of discharge is linked to the positive electrode passivation, an electrolyte having high solvation ability reduces the polysulfide precipitation and delays the positive electrode passivation.
However, the ratio of electrochemical polarization to concentration polarization at the end of discharge (ηe/ηc)e increases with discharge current density.
The battery discharges at constant current rates of 20 Amp, 40 Amp, 60 Amp, and 80 Amp, and the experimental temperature contours are then plotted between the beginning and end of discharge cycle.
Charge/discharge curves of the cell, positive and negative electrodes show that the rapid fall in cell voltage is due to the drop of positive potential caused by depletion of Br2 dissolved in the catholyte at the end of discharge.
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As an illustrative example, both the predictive BCRLB concept and the proposed design methodology are applied to the problem of End-of-Discharge (EoD) time prognostics in lithium-ion batteries.
It indicates that, at the same discharge rate, the batteries' voltages displays significant differences towards the end of the discharge period after different cycle numbers.
For the cell containing the ZFO-200 negative electrode, both electrodes are approaching their full discharge (center plot of Figure 3c) and thus the LFP-CNT electrode voltage is steeply decreasing toward the end of the discharge.
Near the lower end of the discharge nozzle, three-dimensional swirling flows and flow separation are evident.
The most noteworthy surface temperature distribution is observed to be 58.1 °C towards the end of 4C discharge.
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