Hi,
I have to specify and purchase a direct fired 50% glycol heater. There is an existing glycol heater (built in 1960s) in the plant, which is designed per ASME Section I.The design conditions are 75PSIG @ 300oF, with 'S' Stamp on it. My question is, does it qualify as a boiler and must be...
Thanks for your replies, i dont think that its different from the pipeline,I calculated it according to API RP 14E. but someone senior told me that it will be different, thats why i was not sure.I couldn't find it in ASME VIII or B31.3. I found research papers " Erosion in Elbows in HC...
I have to calculate erosional velocity through an inlet nozzel of a flare knock out drum. I am not sure if it has to be calculated the same way as we calculate for the pipelines. Can someone give me some tips/ or reference where i can find the related information.
thanks