NYX,
You should be able to estimate the number of cycles of your system according to the process information that you have. I don't know of any tables to do this. Talk to your process engineering people.
In Caesar II it is customary to use the full pressure in computing pressure thrust. Whether you should turn on this directive or not in the WRC-107 module depends on how your piping is restrained. If you have an anchor or axial stop in the line leaving the nozzle before or at the first bend or tee encountered then you do not need to consider pressure thrust as the nozzle will not be able to pull away from the vessel. Of course, this may cause expansion load problems. If your system has no axial restraint between the nozzle and a pipe bend or tee then you should include the full pressure for determination of pressure thrust.
When the straight run of pipe leading out of the nozzle is of sufficiently long length (I cannot be specific here) then the pipe flexibility may absorb some of the pressure thrust effect, thereby lowering the radial load at the vessel/nozzle interface. I think this is what you are referring to above, but I don't know of a method to calculate this. Perhaps one of our esteemed experts who often post to this forum will have some ideas for you.
Another instance where the vessel shell only sees a portion of the pressure thrust is where you have an axial stop with a gap that is less than the movement the pipe would experience due to pressure at a tee or bend. You could probably estimate the equivalent pressure with Caesar II by calculating the pressure thrust force (P*A), inputting this force for different values of P as an axial force at the first bend or tee, and then running a F1 (OPE) load case and look at your axial displacement at the stop location. Of course, when you do this you should not be modeling the stop. You could then graph your axial displacement against pressure thrust to determine what axial force corresponds to the gap to be modeled in your axial stop. Divide by the internal area of the pipe to obtain the corresponding equivalent pressure. It would not be conservative, but you could use this pressure in your WRC-107 analysis. However, do not use this reduced pressure in your actual static analysis! Use your actual operating conditions and put the stop with gap into the model for the static analysis.
As for which load cases consider corrosion allowance and which do not this depends entirely on which piping code you are considering. Read the specific code you are designing to for the answer to this question.
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