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                                       15     2.0    2.5    30
                                           Safety  laclor
           Figure 15.7 Safety factory vs. fi and PF.

           It must be pointed  out that the calibrated safety factor is usually higher than  the practical
           applied  safety  factor.  For  instance,  it  is  generally believed  that  the  target  safety  level
           according to existing code is lo4, while calculation of the implied safety of the existing rules
           demonstrated  that  the  implied  safety  level  in  the  existing codes  is  of  lo3. A  necessary
           modification based on  practical engineering judgement should be  applied to the calibrated
           safety factor. The history record of safety factor for the considered pipe should be considered
           in the judgement.


           15.6  Conclusions
           A new methodology for fracture assessment of dented pipes with cracks is developed in this
           chapter. The calculated fracture strengths are compared with test data and a good agreement is
           observed. Uncertainties involved in  the  evaluation  are  assessed and  measured.  A  fracture
           reliability model  is  established and  applied to  evaluate  a  practical  existing pipe  further.
           Detailed parametric studies is conducted. A new design equation for dented pipes with cracks
           in operation with  respect to fracture criterion is derived, and corresponding safety factor is
           calibrated based on reliability methods. The methodology presented in this chapter has been
           used in practical engineering and also accepted by the third party verification.


           In  order  to  increase  the  confidence in  the  estimated reliability,  more  refined  statistical
           presentation of  random variables in the analytical model will surely be required, especially
           data from pipe field operation. Other failure modes should be investigated in separate studies
           and  additional information on  pipe  conditions should be  incorporated into the  analysis to
           produce much more practical, safe and economic results.


           15.7  References
           1.  AFT  5L Specifications, American Petroleum Institutes, (1993).
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