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What is the difference between MAWP and MaOP 3 - Eng-Tips
Mar 1, 2004 · maop = 50 psig maop with 20% spike = 1.2 x 50 = 60 psig Assuming we do want to set the relief valve = MAWP (same as Design Pressure): 60psig/0.9 = 66.7 (say 70 psig). So the minimum is 70 psig - what is the maximum? The pipe system is rated for 150 psig maximum - so that s the maximum.
Eng-tips.comMAWP and MAOP - Chemical process engineering | Eng-Tips
Oct 27, 2008 · Except for that unique emergency , some codes limit maop to 15% for less than 1% of the time ( as with safety valve lift events or pump dead head events). In these above cases , Pd is the design pressure based on code calcs and as-recieved pipe or vessel wall thickness and valve or fitting class, whichever is less.
Eng-tips.comMAOP < Design Pressure ??? - ASME (mechanical) Code Issues …
Sep 7, 2007 · I am using Ultrapipe to determine de remaining strength of a corroded pipeline. ASME B31.G compares the maop with the safe maximum pressure for the corroded area. But, Ultrapipe compares this last pressure with the Design Pressure. Is the Design Pressure always greater than the maop? Is that why Ultrapipe uses the DP instead of the maop?. CorpMex.
Eng-tips.comOperating at 1% above MAOP, down stream of compressor …
Jul 8, 2010 · section 7.2.1.2 maop under steady state conditions - For pipelines intended to be operated at a set point equal to maop, the control system shall controll the maximum pressure within a tolerence of 1% further the standards comment on transient pressure at any point in the pipeline shall not eexceed 110% of maop.
Eng-tips.comFinite Element Analysis to compute MAOP of corroded pipeline
Feb 21, 2018 · Barlow's or B31G gives maop much lower than desired maop. [Desire maop 5,000 psi, computed maop based upon Barlow's 3200 psi]. Company hired a high flying engineering consulting company with top brain to show that the pipeline is still good for 5,000 psi based uon their Finite Element Analysis [FEA].
Eng-tips.comMAOP formula - Pipelines, Piping and Fluid Mechanics …
May 7, 2011 · It really depends on where you are (what country, are you inside of plants or outside, are you going through a city or out in the country, is the old pipe seamless or something with a weld seam, etc). The answers all play into the maop or MAWP calculations. Barlow's formula is often part of the calculation, but usually it isn't the first step.
Eng-tips.comClarification on Compressor Station MAOP - Eng-Tips
Feb 13, 2009 · A compressor station design maop is 2500-psi; yet, DOT 192.169 (a) states each compressor station must have pressure relief or other suitable protective devices of sufficient capability and sensitivity to ensure that the maximum allowable operating pressure of the station piping and equipment is not exceeded by more than 10 percent.
Eng-tips.comMAOP and Design pressure difference - Eng-Tips
Oct 13, 2019 · I understood that maop is a limit set, usually by a gornment body, which applies to compressed gas pressure vessels, how can I get this set limit in order to design gas pipeline, PMS pipeline? 2. I understood the design pressure is 10% - 25% higher than maop, how come then that is design has Opreting pressure (kg/cm2g) and the design pressure is 10.55 (kg/cm2g)?
Eng-tips.comMOP-MAOP-MAWP-DESIGN PRESSURE - Chemical process …
Nov 10, 2010 · MAWP and maop are the same thing. Design pressure is a less formal term that sometimes means "design point" or the nominal operating pressure that the system will operate at most of the time (
MAOP of a 6" SS Pipe - Pipelines, Piping and Fluid Mechanics
Jun 3, 2016 · So, moving on to test pressure and maop, tell me if I get this right because I don't know if there are various grades of SS pipe like there are CS pipe (i.e. Gr. B, x42, x46, etc.) For a 0.280 wall SS pipe, the max allowable working pressure is 2187 psig. So that puts us at 100% of SMYS for a design factor of 0.5 of 4374 psi.
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