HI KAKAIE:
Are you content?, that is enough?
My summary is: Basic design goes up to process design (you understand process design'): Flows, operating conditions, size of equipments, budget costematings, etc. Detailled Dsgn covers all details of piping and all works,
NOROS
I have a software for that calculation.
Please give me your data: TBP curve, KUOP.
Crude API gravity, viscosity at 100ºF, viscosity at 210ºF
My software is based in Edmister Method to get yields of gasoline, naphtha, kerosene, etc.
I'm waitig for you
Do you need a software or only the ecuation to calculate the pressure drop.
Condenser calculations are different for gasoline than propane. What type of hydrocarbon are you condensing?.
If you give me datas y would help you.
I need flow inside tube, inlet temperature, fluid name or phisical...
Most, refinery heaters are designed with natural draft (almost all negative pressure in radiant and convection), if these heater have positive pressure in any part of the heater, the flue gas will leak through heater case, then you will not able to control the excess air (then efficiency)...
