Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations KootK on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Uprating Gas Pipe by ASME 31.8

Status
Not open for further replies.

arielrulo

Petroleum
Aug 10, 2012
1
Dear All

I would like to shear an interpretation I am doing about ASME 31.8 and hear your opinion. (All references from now on is for ASME 31.8 2018 Edition)

I have this Gas pipe installed:
12 in – API 5 L Gr 70 – e: 7.9mm
Design pressure calculated by 841.1.1 is 102.9 kg/cm2g calculated with:
S = specified minimum yield strength 70000 psi
D = nominal outside diameter of pipe 12.75 in
E = longitudinal joint factor 1
T = temperature derating factor 1
t = nominal wall thickness, in. 7.9mm – 3.2mm corrosion allowance: 4.8mm (0.185in)
Hydraulic test pressure done at 99x1.25 kg/cm2g. By table 845.2.2-1 maximum operating pressure is 99 kg/cm2g.
Now well, we need to operate at 108 kg/cm2g to avoid high operations cost and is unviable to do a new hydraulic test.
So we change our design (change corrosion allowance to 1.6mm)
New maximum operating pressure calculated 137.9 kg/cm2g BUT we are limited by hydraulic test that has been done at 124 kg/cm2g. So by table 845.2.2-1 maximum operating pressure is hydraulic test divided 1.25, 124 / 1.25 : 99 kg/cm2g
Now based on 857 Uprating part of code.
Item 851.1.c) is totally accomplish.
Now we see 857.2 d) and base on that article marked on yellow (see atached file) i think we can operate at 108 kg/cm2g

What do you think about this interpretation?

Thanks in advance,
Ariel
 
 https://files.engineering.com/getfile.aspx?folder=bfce905a-6424-4b09-9502-f235fd8aa6ef&file=857.2_d).JPG
Status
Not open for further replies.

Part and Inventory Search

Sponsor