BradyJr
Mechanical
- Oct 24, 2016
- 8
Hello,
I normally work with ASME Section VIII Div 1 but was asked to perform the ASME Section VIII Division 2 -Fatigue Screening (5.5.2.3) on a pressure vessel and I'm trying to sure up my understanding of the screening. Hopefully someone on here has some experience and wouldn't mind sharing their knowledge.
1. Step 2 asks to determine the expected (design) number of full-range pressure cycles. What exactly qualifies as a 'full-range pressure cycle'? Is it when the pressure reaches the design pressure, how many times if returns to be pressurized, or just a cycle. My case in particular has two cycles which are performed one after another. Cycle 1 is a 9.9 kg/cm^2 and cycle 2 is at 10.5 kg/cm^2 with no fluctuations during the cycles. The design pressure is 19.5 kg/cm^2. My current interpretation that a 'full-range pressure cycle' would only occur at startup and shutdown.
2. Step 4 asks to determine the effective number changes in metal difference between any two adjacent parts. The pressure vessel is made of all group 1 carbon steel and the process fluid has access to of the vessel components from the inside so I do not anticipate much of a temperature gradient among components (FEA shows well below 28 C differential). My current interpretaion of this is that NΔTE would be zero?
Any insight or suggestions would be much appreciated.
Thanks
I normally work with ASME Section VIII Div 1 but was asked to perform the ASME Section VIII Division 2 -Fatigue Screening (5.5.2.3) on a pressure vessel and I'm trying to sure up my understanding of the screening. Hopefully someone on here has some experience and wouldn't mind sharing their knowledge.
1. Step 2 asks to determine the expected (design) number of full-range pressure cycles. What exactly qualifies as a 'full-range pressure cycle'? Is it when the pressure reaches the design pressure, how many times if returns to be pressurized, or just a cycle. My case in particular has two cycles which are performed one after another. Cycle 1 is a 9.9 kg/cm^2 and cycle 2 is at 10.5 kg/cm^2 with no fluctuations during the cycles. The design pressure is 19.5 kg/cm^2. My current interpretation that a 'full-range pressure cycle' would only occur at startup and shutdown.
2. Step 4 asks to determine the effective number changes in metal difference between any two adjacent parts. The pressure vessel is made of all group 1 carbon steel and the process fluid has access to of the vessel components from the inside so I do not anticipate much of a temperature gradient among components (FEA shows well below 28 C differential). My current interpretaion of this is that NΔTE would be zero?
Any insight or suggestions would be much appreciated.
Thanks