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JPE - Sept09 - cover2-4.pmd - Pipes & Pipelines International ...

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180<br />

Crack Mouth Opening Displacement (inches)<br />

0.004<br />

0.003<br />

0.002<br />

0.001<br />

δ<br />

0.1 mm<br />

a<br />

σ<br />

t<br />

σ<br />

0.000<br />

0 500 1000 1500 2000 2500<br />

cracks under either the MAOP or an external soil load that<br />

will yield the entire pipe, an analysis must be performed to<br />

evaluate the crack opening for such cracks under such<br />

loads.<br />

To put an upper bound on the crack mouth opening<br />

displacement (CMOD), the crack geometry is taken as the<br />

crack shown in Fig.6 with the pipe cracked all the way<br />

around the circumference of the pipe. The solutions were<br />

performed for a pipe with R/t = 18.2, a hardening exponent<br />

of n = 10, and different depths into the wall (see Fig.6). This<br />

solution should slightly overestimate the crack opening of<br />

a finite length crack in the actual pipe since the crack is not<br />

all the way around the circumference of the pipe.<br />

Figure 6 shows that under the design operating pressure of<br />

2,700psi (72% SMYS), even a crack that has propagated<br />

halfway through the wall is not reliably detectable by the<br />

MFL technique, since the crack mouth opening is still less<br />

than 0.1mm. At an assumed operating pressure of<br />

approximately 2,320psi a circumferential crack that is 15%<br />

of the way through the wall would have a crack mouth<br />

opening that is an order of magnitude less than the detection<br />

limit of the MFL technique.<br />

In this context it is also useful to consider what the crack<br />

mouth opening displacement would be under both the<br />

operating pressure and external loads such as soil loads.<br />

The CMOD versus applied bending moment and versus<br />

applied tension with the same crack configurations and<br />

pipe geometry as given in Fig.6 are plotted in Figs 7 and 8,<br />

respectively. In both cases the applied load is in addition to<br />

the operating pressure of 2,320psi (86% of the MAOP).<br />

a<br />

Internal Pressure (psi)<br />

a=0.15t<br />

a=0.25t<br />

a=0.5t<br />

Cracked Region<br />

t<br />

Operating<br />

Pressure<br />

The Journal of Pipeline Engineering<br />

The loads at which the cracks could fail by plastic collapse<br />

of the remaining ligament are circled in red in Figs 7 and<br />

8: when the crack is 15% of the wall thickness, an external<br />

soil load of 720kips would cause the remaining ligament to<br />

reach the flow stress (76,000psi) of the material. At this<br />

point the crack opening is only 0.03mm and below the<br />

detection capability of the MFL technique. When the crack<br />

is 25% of the wall thickness, an external soil movement<br />

inducing a tensile load of 595kips would cause the remaining<br />

ligament to reach the flow stress (76,000psi) of the material.<br />

At this point the crack opening is only 0.06mm, which is<br />

still below the detection capability of the MFL technique.<br />

Therefore the MFL tool is most likely not capable of reliably<br />

detecting this size of circumferential cracks prior to them<br />

being susceptible to progressive tearing by small increases<br />

in external loadings.<br />

Sample issue<br />

Fig.6. Plastic CMOD of an outside<br />

circumferential for three different<br />

crack depth versus internal pressure<br />

for a pipe with dimensions R/t =<br />

18.2 and t = 0.375in.<br />

The repeat inspection interval required to mitigate this risk<br />

is determined by computing the difference between the<br />

time to detection, T det , i.e., the amount of time needed<br />

under the loading conditions for the crack to grow to a<br />

detectable size at high probability and confidence for the<br />

chosen method, and T c , the time needed under the loading<br />

conditions for the crack to grow to a critical size. This gives<br />

rise to the computation of the safe inspection interval T s ,<br />

which is simply the difference T c - T det . The repeat inspection<br />

interval is then typically chosen to be a fraction of this the<br />

safe inspection. If the length of time is short between when<br />

the crack can be detected and when the crack is critical, a<br />

short repeat inspection interval is obtained that would be<br />

economically and logistically not viable.<br />

Following the above, it is imperative that pipelines in

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