Increasing ambient temperatures in inland locations has meant that triethylene glycol (TEG) absorbers used to dehydrate raw natural gas may need to operate at temperatures of up to 60 °C. These higher temperatures may lead to increased TEG slippage into the downstream gas, but the extent of this slippage is not readily estimated due to a lack of appropriate vapor−liquid equilibrium data. In this work, new laboratory data for the gas phase concentration of triethylene glycol (TEG) in highpressure methane (CH 4 ) are presented, at pressures of up to 134 bar and temperatures of 40, 50, and 60 °C. The new data are consistent with published data for TEG solubility in high-pressure CH 4 at lower temperatures and are readily described by a Cubic-Plus-Association (CPA) model using existing model parameters. The CPA model yields an average absolute relative deviation (AARD) of 53% relative to the new experimental data when a binary interaction parameter of 0.136 is used, and this increases slightly to 57% when the literature value of 0.1643 is used.