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Stable Charge/Discharge Cycle Performance of LiFePO4 Cathode Prepared with Carboxymethly Cellulose Binder
The Al foils used as current collectors are 99.99% pure with a 100-μm thickness. The chemical treatment of Al foils was referred to in Japanese patents acquired by the Japan Surface Treatment Institute Co., Ltd. 1,2 All slurries were prepared using Milli-Pore water (> 18 MΩ). The CMC1 (degree of etherification = 0.7, viscosity = 1000–2000 mPa·s at 1% AQ, 25 °C) binder purchased from Polyscience Inc., the CMC2 (CMC-2200, degree of etherification = 0.8–1.0, viscosity = 1500–2500 mPa·s at 1% AQ, 25 °C) binder received from Daicel, Japan and the polyvinylidene difluoride (PVdF, KF9130, Kureha, Japan) were used as received without any further treatment to prepare the LiFePO4 cathode. To avoid agglomeration of the cathode material and binder in the cathode film, the mixture containing the LiFePO4 active material and acetylene black was first dispersed in water; then, a CMC aqueous solution was added to this suspension, and the mixture was subsequently magnetically agitated for at least 4 h prior to producing the electrode film. The cathodes were prepared via doctor-blade (100-μm gap) coating. Electrochemical tests were performed using a CR2032 coin-type cell. The test cell was comprised of a cathode and a lithium metal anode separated by a porous polypropylene film (Celgard 3401). The electrolyte used in the tests contained a mixture of 1 M LiPF6-ethylene carbonate (EC)/dimethylcarbonate (DMC) (1:2 v/v, Ube Chemicals, Japan). All tests were performed at room temperature. A constant-current (CC) mode was applied to the pre-treatment process and cycle tests.
The cathodes prepared with the chemically treated Al foils exhibited a stable charge/discharge capacity for 100 cycles compared with the mechanically treated Al foils that exhibited poor stability in their charge/discharge capacity (Fig. 1). Two of the CMC samples ((a) and (b)) did not exhibit a large difference in their cycle performance, indicating that the degree of etherification and viscosity of the CMC affects the cycle performance. The charge capacities observed during first several cycles were below the stable charge/discharge capacities after several cycles. The decrease in the initial charge capacity can be explained by the deintercalation of the Li+ ions from the LiFePO4particles during their exposure to the aqueous solutions used to prepare the slurry containing the CMC binder. The rate performance is important in the application of LiFePO4 cathodes. All cells were charged at a current of 0.1 C to insure identical initial conditions for each discharge. The discharge currents were 0.1, 0.2, 0.4, 0.8, 1.6 and 3.2 C, indicating that the LiFePO4cathodes prepared with CMC1 and CMC2 exhibit discharge capacities comparable to those obtained using a conventional PVdF binder even at high rate current. Therefore, the CMC binders do not exhibit and negative influence on the rate performance.