Investigation of manufacturing parameters for NaCl–Ni granule type cathodes used in low temperature NaSICON sodium-metal chloride batteries
Introduction
Sodium-metal chloride battery (Zebra battery) is a promising candidate for grid energy storage and electric vehicle applications due to its high energy density, high durability and zero self-discharge [1], [2], [3], [4], [5], [6]. Although the Zebra battery is already pre-commercialized by FIAMM SoNick and General Electric, many researchers are still investigating advanced technologies for enhanced performance, long-term durability and cost competiveness [7], [8], [9], [10].
The low temperature operation (below 200 °C) of Zebra battery is fairly attractive to obtain longer life cycle and low-cost construction materials (sealant, metal parts) [8], [11]. To get appropriate battery performances at low temperature below 200 °C, significant efforts should be focused on reducing internal resistance contributed by the solid electrolyte, negative/positive electrodes and metal current collector parts. In particular, NaSICON (Na1+xZr2SixP3-xO12) materials have attracted significant interests as a promising solid electrolyte for low temperature sodium rechargeable batteries due to its high ionic conductivity of 0.15–0.2 S/cm−1 at 200 °C which are comparable to that β”-Alumina at 260 °C [3]. In addition to the preliminary reports that reveal the high stability of NaSICON in molten sodium and molten salt electrolyte [12], [13], [14], the researchers recently reported the low temperature Zebra battery using NaSICON which are successfully operational at 195 °C [15].
To get further improvement in cell performance, thorough investigations are necessary in cathode development to get an optimum composition, microstructure and geometry. Zebra battery is typically fabricated in a discharge state and the initial cathode material is composed of transition metal chlorides and excess metals. There are a few literature reports regarding cathode development which deal with the composition control [4], [16], [17], [18] and manufacturing conditions [4], [19], [20], [21]. Although cathode materials for Zebra batteries can be prepared by various processes to have diverse shapes and microstructures, the major commercial players have focused on developing granule-type cathodes due to their advantages in manufacturing simplicity and cost [4], [8], [16], [19], [20].
Roll compaction is a proven dry-granulation process in pharmaceutical industry for producing fine powders in order to improve the fluidity and homogeneity of powder mixture, so that it can be handled easily [22]. In Zebra battery industry, this roll compaction seems to be advantageous in manufacturing high capacity cells by simply filling them in the cathode volume through a small hole. Furthermore, another benefit of the granule-type cathodes is fabrication of Zebra cells with diverse shapes regardless of cell design due to its high fluidity. However, no publications and patents were reported so far to explain the manufacturing processes of granule-type cathodes used in Zebra battery.
In this work, the researchers have studied to find out key parameters to manufacture high-quality cathode-type granules using a dry roll compaction method that enables the optimal electrochemical performance of Zebra battery at 195 °C. The roll compaction conditions were controlled as key influential parameters which determine the size, shape and pore structure of the granules. The optimum processing condition for the granule-type cathodes was discussed considering electrochemical performance in unique cell tests with a self-developed Zebra cell configuration with NaSICON solid electrolyte membrane. The long-term performances of the cells using stable granule-type cathodes were evaluated with the consideration of cathode characteristics and NaSICON stability.
Section snippets
Cathode preparation
Initially, fine size (<45 μm) of NaCl and FeS2 (<100 μm) powders were obtained by a dry planetary ball mill (PULVERISETTE 5/4 classic line, FRITSCH) at 1000 rpm for 1 h. Zirconia beads with 1 cm diameter were used (NaCl/ball weight ratio = 1/2.5) as grinding media. The cathode powder mixture was prepared to have a precise composition (Ni/Fe/NaCl molar ratio = 1.5/0.3/1, FeS2 1.87 wt%, NaI 1 wt%) by homogenous dry mixing of NaCl (Sigma–Aldrich, 99.5%), Fe (Sigma–Aldrich, 99.5%), Ni (Vale, type
Results and discussion
ICP analysis was carried out to confirm the homogeneity of as-synthesized molten salt electrolyte as shown in Table 1. It was revealed that the molar ratio of Na to Al is 0.526:0.473, which quite corresponds to the target ratio of 0.53:0.47.
Fig. 2 exhibits the X-ray diffraction (XRD) pattern of as-synthesized NaAlCl4 salt powder at room temperature. The XRD pattern of as-synthesized molten salt revealed the formation of crystalline phase of NaAlCl4 with orthorhombic structure (JCPDS No.
Conclusion
The manufacturing parameters were controlled to determine the optimum processing condition of NaCl–Ni cathode granules for sodium-metal chloride batteries. It was discovered that the optimum roll speed and pressure were essential to produce stable granule-type cathodes for efficient electrochemical performance. The high roll speed (2.5 rpm) was revealed to produce thin and fragile granules (B, D) causing a dramatic increase of ohmic cell resistance. The rise of ohmic resistance in cathodes is
Acknowledgments
The authors acknowledge a grant-in-aid from SK innovation supported by Ceramatec, Inc. for NaSICON development.
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