Bill3752
Chemical
- Jan 24, 2008
- 138
I am evaluating installation of a bidirectional RD. To properly calculate the capacity of the RD and related piping I need an estimate of the Kr and MNFA of the candidate RDs. However, this is not an ASME application (MAWP<15 psig and MAEP = -8 psig). I remember running across some documentation some years ago to use Kr = 1.5 when one doesn't have a certified value, but I don't remember for sure.
I can't apply the original Kd = 62 method.
Any input would be appreciated.
I can't apply the original Kd = 62 method.
Any input would be appreciated.