Solubilities of Ethylene and Carbon Dioxide Gases in Lithium-Ion Battery Electrolyte

Abstract

During Li-ion battery operation, (electro)chemical side reactions occur within the cell that can promote or degrade performance. These complex reactions produce byproducts in the solid, liquid, and gas phases. Studying byproducts in these three phases can help optimize battery lifetimes. To relate the measured gas-phase byproducts to species dissolved in the liquid-phase, equilibrium proprieties such as the Henry’s law constants are required. The present work implements a pressure decay experiment to determine the thermodynamic equilibrium concentrations between the gas and liquid phases for ethylene (C₂H₄) and carbon dioxide (CO₂), which are two gases commonly produced in Li-ion batteries, with an electrolyte of 1.2 M LiPF₆ in 3:7 wt/wt ethylene carbonate/ethyl methyl carbonate and 3 wt % fluoroethylene carbonate (15:25:57:3 wt % total composition). The experimentally measured pressure decay curve is fit to an analytical dissolution model and extrapolated to predict the final pressure at equilibrium. The relationship between the partial pressures and concentration of dissolved gas in electrolyte at equilibrium is then used to determine Henry’s law constants of $k_{C_2{H}_4}=$ 2.0 × 10⁴ kPa for C₂H₄ and k_CO2 = 1.1 × 10⁴ kPa for CO₂. These values are compared to Henry’s law constants predicted from density functional theory and show good agreement within a factor of 3.