Calculation of stable systems

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Hello everyone. The absorption tower in the device’s absorption and stabilization system is not able to effectively absorb the components in the dry gas that are above C3; the concentration of these components exceeds the allowed limit by 10% (v/v). However, I now want to conduct calculations on the absorption tower, but since the absorbent used is stabilized gasoline, I am unable to determine the dissolution levels of dry gas, liquefied gas, etc., within the gasoline. I would like to ask the experts: How does one calculate the use of gasoline as an absorbent to absorb enriched gas (a mixture of dry gas and liquefied gas)? Now I am considering using the available analysis data to calculate the dissolution of rich gas (a mixture of dry gas and liquefied gas) in stable gasoline. Calculating. Ask again if there are any methods to directly determine the K (phase equilibrium) value