Hello,
I seem to remember reading somewhere that PSVs may be set 10% above piping MAP, as ASME B31.1 allows up to 20% overpressure of flanged piping for short durations. Has anyone else read this somewhere or did I just imagine this? Anyone have a code reference on this?
I am interested in...
thread483-301005
Given lean amine simulation stream shows:
0.00148 mol H2S / 0.0869 mol DEA
H2S MW = 34.081 g/mol
DEA MW = 105.14 g/mol
DEA density = 1097 g/L
This implies a lean amine acid gas loading of about 6.06 g H2S / L DEA, but the lab data is showing this stream should be about 0.16...