Hello my colleagues! There is anyone who have an experiance of simulation gas procesing plant with propane refrigeration unit?

I have a question about recuperator heat exchanger design and chiller (evaporator) design.
Typically we need less flowrate of methanol to prevent hydrate formation in coparison with using glycols. Features of methatol and EG are different (viscosity etc).
I accume that in case of using EG the heat transfer area of HE and chiller needs more large than in case of using methanol.
So my question is how much times (percents) the heat transfer area of HE and chiller are approximately larger in case of using EG?