pleckner,
check this one for reference. If you get it may be u find interesting.
http://webwormcpt.blogspot.com/2007/08/discussion-on-isentropic-and.html
Hello all expertise,
I am trying to understand slip flow methods (models) for two phase discharge, like fauske, moody and many others. Are there any guideline available for selection of methods or any other reference.
Thank you
Thank you Pleckner and Latexman,
Pleckner,
If i m not misunderstanding it, than beta should be high (in our case isn't it should be equal to 1 (d2=d1), technically its not orifice but pipe exit).
let me know if i m getting it wrong and sorry if i m going in wrong direction.
Latexman,
I will...
Thank you Pleckner and Latexman,
PLECKNER,
My tube ID is .782" and Shell ID is 58". But i am not able to figure it out how to get C value. Either it has some trick or i am not able to figure out simple way to read graph. If you can guide me i will really appreciate.
Latexman,
Shell sibe...
Thank you Latexman for your quick reply and sorry for not providing much information.
MAWP Tube side (cooling water): 150 psig and operating 135 psig
MAWP Shell Side: 65 psig and operating around 52 psig
So, i think catastrophic failure is a possible scenario.
If i am not wrong Equation 3-21...
I have cooling water tube rupture case, and i am not able to find the flow to shell during tube rupture. I tried to find in crane, but it didn;t help me.
Please let me know the way to calculate flow.
Thank you,
Harshal
