10 October 2023 1 8K Report

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?

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