钒
五氧化二铁
电解质
流动电池
溶解
无机化学
氧化还原
硫酸
电化学
阳极
化学
磷酸钒锂电池
电池(电)
材料科学
电极
热力学
物理化学
功率(物理)
物理
作者
Janet L. Martin,Katharina Schafner,Thomas Turek
标识
DOI:10.1002/ente.202000522
摘要
The vanadium redox‐flow battery is a promising technology for stationary energy storage. A reduction in system costs is essential for competitiveness with other chemical energy storage systems. A large share of costs is currently attributed to the electrolyte, which can be significantly reduced by production based on vanadium pentoxide (V 2 O 5 ). In this study, the dissolution kinetics of V 2 O 5 in diluted sulfuric acid and commercial vanadium electrolyte (VE) is determined. The low solubility of V 2 O 5 in sulfuric acid can be overcome by partially using VE with a state of charge of −50% as solvent. In this way, a complete dissolution of V 2 O 5 is possible within ≈10 min to achieve the desired vanadium concentration of 1.6 mol L −1 . Moreover, the electrochemical reduction of an electrolyte containing VO 2 + coupled with the oxygen evolution reaction at the anode is investigated. For these consecutive steps, an electrical energy demand of 1.69 kWh kg −1 is required to reach a state of charge of −50%. Finally, both processes are integrated into a plant concept for continuous electrolyte production.
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