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pressure relief valve settings per ASME SEC VIII div 1

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Dec 21, 2018
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Just to confirm my beliefs; The maximum set point of a PRV on a vessel with one PSV installed is the MAWP. The MAWP is defined as the maximum pressure calculated on a vessel using nominal thickness, exclusive of corrosion allowance. Therefore let us say that we have a 100" diameter shell with 0.375" thick material with 20,000 psi allowable stress, JE=1. I calculate a MAWP of 149 PSIG and this is the highest i can set the PRV? accounting for static head, of course
 
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If the stamped MAWP is 149 psig, then the maximum set pressure for a single relief device is also 149 psig
 
MAWP calc should INCLUDE corrosion allowance. Others may comment on caveats re the JE=1.0.
 
A great question to post on the "Safety Relief valve" forum ....

MJCronin
Sr. Process Engineer
 
Exclusive in this context means "not including".

Regards,

Mike

The problem with sloppy work is that the supply FAR EXCEEDS the demand
 
Nom. Thickness includes CA....would be .375" - CA for MAWP
 
pressure equipment engineer said:
I calculate a MAWP of 149 PSIG and this is the highest i can set the PRV? accounting for static head, of course
MAWP is defined as the pressure at the top of the vessel, no need to account for static head.
 
"Not including" means CA is deducted from the nominal thickness for calculations. Code dimensions including thicknesses are nearly always less the CA and any applicable tolerances. See U-5, UG-16(e). The term "nominal" is used to distinguish from "required", etc.

Regards,

Mike

The problem with sloppy work is that the supply FAR EXCEEDS the demand
 
Lets check the issue with another point of view!
from HRSG basic design point of view we normally first define the design pressure of the vessel/drum based on the maximum operating pressure, then this design pressure will be the MAWP of the vessel/drum.
after defining the MAWP of the drum thickness and other characteristics will be calculated.
 
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