Put everything in the gas analysis in terms of mass fraction, then convert the gas flow rate to mass basis. Take out the mass of Water, Methane, Carbon Dioxide, Nitrogen, Hydrogen Sulphide and other non-condensibles. The rest ought to be what is available to you to produce liquids. You would then likely need to adjust for a recovery efficiency, as stated in the above posts. The remaining consideration is then to determine if you are trying to produce NGL (which has a product specification based on constituent fractions) or stabilized condensate (which has an RVP specification) or both.
Regards,
SNORGY.