I think carbon dioxide will liquify at pressure between 5 and 74 bar and temperature between -56 to 31 degC. At a pressure of 46 bar methane is a gas and above 46 bar it is in supercritical state.
Is it possible to do a gas liquid separation when methane is either in subcritical or supercritical state? But also retain the pressure in the separated methane gas product?
I am wondering if anyone has investigated this as an alternative method of biogas upgrading? where two products of carbon dioxide and methane are recovered as pressurized products to minimise energy loss?