Page 51 - Pipeline Risk Management Manual Ideas, Techniques, and Resources
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                         Conditions *-------------------------------------
                                                                       + Actions
                                 Figure 2.3  Example items on attributes-preventions  scale.


          the environment of the section-harsh  conditions require more   The range should include the smallest to largest values in sys-
          preventions to meet the standard.           tems to be studied as well as future systems to be acquired or
                                                      other systems that might be used as comparisons.
          Model scope and resolution                   Given the difficulties in predicting future uses of the model,
                                                      a more generic  model-widely   applicable to many different
           Assessment  scope  and  resolution  issues  further  complicate   pipeline systems-might  be appropriate.
           model design. Both involve choices of the ranges of certain risk
           variables.  The  assessment  of  relative  risk  characteristics  is   Special Risk Factors
           especially sensitive to the range of possible characteristics in
           the pipeline systems to be assessed. If only natural gas trans-   Two possible risk factors deserve  special consideration  since
           mission pipelines are to be assessed then the model does not   they have a general impact on many other risk considerations.
           necessarily have to capture  liquid pipeline variables  such as
           surge potential. The model designer can either keep this vari-   Age as a risk variable   Some risk models use age as a risk
           able and  score  it  as “no  threat”  or she  can  redistribute  the   variable. It is a tempting choice since many man-made systems
           weighting points to other variables that do impact the risk.   experience deterioration that is proportional  to their years in
            As another example, earth movements often pose a very local-   service. However,  age  itself  is not  a  failure  mechanism-at
           ized threat on a relatively few stretches of pipeline. When the vast   most it is a contributing factor. Using it as a stand-alone risk
           majority  of a pipeline system to be evaluated is not exposed to any   variable can detract from the actual failure mechanisms and can
           land movement threats, risk points assigned to earth movements   also unfairly penalize portions of the system being evaluated.
           will not help to make risk distinctions among most pipeline seg-   Recall  the  discussion  on  time-dependent  failure  rates  in
           ments. It may seem beneficial to reassign them to other variables,   Chapter  1, including  the  concept  of the bathtub  failure  rate
           such as those that warrant full consideration. However, without   curve. Penalizing a pipeline for its age presupposes knowledge
           the direct consideration for this variable, comparisons with the   of that pipeline’s failure rate curve.
           small portions of the system that are exposed, or future acquisi-   Age alone is not a reliable indicator ofpipeline risk, as is evi-
           tions of systems that have the threat, will be difficult.   denced by some pipelines found in excellent operating condi-
            Model resolution-the   signal-to-noise ratio as discussed in   tion even after many decades of service. A perception that age
           Chapter I-is   also sensitive to the characteristics of the systems   always causes an inevitable, irreversible process of decay is not
           to be assessed. A model that is built for parameters ranging   an appropriate characterization ofpipeline failure mechanisms.
           from, say, a 40-inch, 2000-psig propane pipeline to a 1-inch,  20-   Mechanisms that can threaten pipe integrity exist but may or
           psig fuel oil pipeline will not be able to make many risk distinc-   may not be active at any point on the line. Integrity threats are
           tions between a 6-inch natural gas pipeline and an 8-inch natural   well  understood  and  can  normally  be  counteracted  with  a
           gas pipeline. Similarly, a model that is sensitive to differences   degree of confidence. Possible threats to pipe integrity are not
           between a pipeline at 1 100 psig and one at 1200 psig might have   necessarily  strongly  correlated  with  the  passage  of  time,
           to treat all lines above a certain pressure/diameter threshold as   although the “area of opportunity” for something to go wrong
           the same. This is an issue ofmodeling resolution.   obviously does increase with more time.
            Common risk variables that should have a range established   The ways in which the age of a pipeline can influence the
           as part of the model design include        potential for failures are through specific failure mechanisms
                                                      such as corrosion and fatigue, or in consideration of changes in
            Diameter range                            manufacturing  and  construction  methods  since the pipeline
            Pressure range                            was  built.  These  age  effects  are  well  understood  and  can
            Products to be included                   normally be countered by appropriate mitigation measures.
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