Theoretical Investigation of Vanadium Crossover Phenomena through Different Types of Membrane in Vanadium Redox Flow Battery

Redox flow batteries (RFBs) as enery storage system are getting much public attention because their power and capacity can be configured independently with relatively low capital investment compared to other types of batteries. All vanadium redox flow battery (VRFB) has an additional advantage of low maintenance cost. In detail, becasue positve and negative electrode of a VRFB share the same active material (vanadium), contaminated electrolyte due to vanadium crossover through membrane can be recycled by rebalancing process. Electrolyte contamination in a VRFB is mainly caused by the amount of vanadium and water crossover through the membrane, which causes capacity decay and power loss accompanied by additional maintenance cost during VRFB operation. The vanadium crossover is controlled by diffusion, migration, and convection across the membrane. It was reported that the following side reactions occur when vanadium ions move to the counter electrode side (1) : It is also known that the water transfer through the membrane is controlled by three mechanisms as follows (2) : 1) Water molecules are transferred along with a vanadium ion that moves to the counter electrode 2) Water molecules are transferred along with a proton to satisfy electro-neutrality 3) Water molecules are transferred by osmosis phenomenon due to vanadium concentration difference between two electrolytes The above vanadium and water transfer through membrane strongly denpends on the physico-chemical properties of the membrane. In this study, we aim to elucidate crossover phenomenon and its consequence in a VRFB by taking computational apporach with a physics-based multi-dimensional VRFB model that has capability of simulating complex species transfer mechanisms. Further, we analyze the cause and effect of each crossover mechanism according to the different types of membranes such as anion exchange membrane, cation exchange membrane, and micro-porous separator. We conclude our study by suggesting electrolyte rebalancing strategies for each type of membrane. References [1] K. W. Knehr, Ertan Agar, C. R. Dennison, A. R. Kalidindi, and E. C. Kumbur, J. Electrochemical Society 159 (2012) A1446-A1459 [2] Chenxi Sun, Jian Chen, Huamin Zhang, Xi Han, Qingtao Luo, J. Power souces 195 (2010) 890-897 Figure 1