well life is comparatively easier if it's an atmospheric Column rather than a Vacuum Column !
Please take care of Following
1.Annular flow Regime is most stable amd most preferable for any General Two-phase flow ,however also check for flow ragimes at turndown flowrates also and advise Mechanical piping group for proper supports.I would also prefer to size line in segments as per varying operating pressure along the length from variousheater passes to the Main tranfser line (however that is more significant in case of vacuum heater/Column)
2.Ensure that pressure drop in the line matches with Furnace Outlet pressure(Infact heater and transfer line hydraulics should be done simultaneously)
if Pressure Drop is higher Builtup backpressure at Furnace Outlet is more than it was designed and hence there are chances of coking
if Pressure Drop is lower that designed Heater Oulet pressure there may be more flashing and increased velocity thereof may erode lines/cause piping supoort issues.
3.Try to minimize the run length ,long transfer lines with many crosses and tee’s will rapidly coke and increase the pressure on the furnace which usually results in increased fouling of the tubes in the furnace.
4.For Design Pressure consideration,Calculate backwards from Column Maximum operating pressure and keep on adding dynamic loss elements.
5.Design Temperature is genreally governed by Heater COT.
Hope this helps,
Regards
Himanshu