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Lithium-Sulfur Battery: Design, Characterization, and Physically-based Modeling

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Lithium-Sulfur Battery: Design, Characterization, and Physically-based Modeling ( lithium-sulfur-battery-design-characterization-and-physicall )

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cycles and can actually lead to a temporary increase of the capacity, cf. e.g. Fig. 3.24. For reasons unknown, the SBR binder used in these cells is often associated with this behavior [161]. Second, a small fraction of the electrons transferred may not contribute to sulfur oxidation, but instead fuel side reactions such as the polysulfide shuttle. This cell configuration does not suffer from the shuttle effect much and consequently, no infinite charging [51, 113] was observed ever. Still, some of the charge capacity might enter this pathway or other side reactions. The voltage trace can also be illustrated differently: Fig. 3.21 shows results of an- other cell, this time plotting voltage vs. the capacity transferred during each half cycle, resetting the abscissa to zero at the end of each charge or discharge. In this represen- tation, each half cycle can be directly compared to the following (or preceding) one. This way, any discrepancy can be spotted and quantified easily. Degradation can be observed by comparing subsequent discharges. To enhance the effect, only every 10th cycle is plotted in Fig. 3.21. 3 2.5 2 1.5 1 10th 20th 40th 60th 80th 99th 120th 140th 160th 180th 199th loading: 1.03 mg/cm2 composition: 80 % Li2 S (coated), 10 % carbon, 10 % SBR 50 % Pyr14 TFSI, 50 % DOL/DME + 1 M LiTFSI, 0.3 M LiNO3 0 200 400 Capacity / Ah/kgS Figure 3.21: Continuous capacity fade over 200 cycles. Charge and discharge at a rate of C/10. The cell voltage is plotted against the capacity transferred during each half-cycle. Besides the capacity fade, the most prominent effect of degradation is the increased voltage hysteresis, which almost doubles during the first 200 cycles for the cell pre- sented in Fig. 3.21. The hysteresis, i.e. the difference in voltage at the same SoC during charge and discharge, is directly proportional to the anergy, i.e. the energy lost as heat during one cycle. The exergy, in contrast, is proportional to the integrated area under the discharge curve and finally, the total work performed is equal to the area under the 60 600 800 1000 Cell voltage / V

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