Portable Occupied Building

[flozzermeister]

Hello all,

Does anyone of you have the latest CCPS guidelines on "Guidelines for Siting of Occupied Portable Buildings in chemical facilities" June 19, 2007.

Alternatively I am using the Baker Strehlow Tang method for modelling VCE overpressure ranges and have interesting results as my process is CH4, pipeline quality. I have done a bit of sensitivity analysis using the 3D flame expansion and 2.5D. 2.5D results are almost double the 3D ones and I am wondering whether the model used by Phast interpolates the results from 2D and 3D as opposed to use blast curves for 2.5D

My volume is about 5000 m3 in piperack with maximum height of 18 metres. Wonder if I can get away using 3D ??

any takes?

[bullseye]

i'm also very interested in this guideline.

can anybody share it?