Imok, check your last post, the 0.0575 can't be right.
The Separation Capacity of a horizontal vessel is going to be very much the same for any 60" Diameter, from any manufacturer, until the pump requirements kick into the equation...So if a reputable manufacturer constructed the package intact and knew its refrigerant, temperature and operating requirements, it will be tall enough that the (original) pumps will have sufficient NPSH at a specific, maintained operating level. An it won't vary much from manufacturer to manufacturer. If the pumps have been renewed and upsized, or if the pump inlet piping was designed with a higher evaporating temperature intended, or if operations require that the liquid level be otherwise run "high", the separation space is being encroached upon...
Providing the pumps have enough flow and pressure, the answer for a purpose-built package should be about 425 TR.