Page 63 - Pipelines and Risers
P. 63

36                                                                Chapter 2


           where:
                 V,  =(S+3*h)*[$*[(Di  +2*t)2-D?!                             (2.33)

           where:
                Vp  = Volume of pipe to be repaired [m3]
                S   = Spacing between buckle arrestors [m]
                h   = Greatest depth in the section considered [m]
                CF    3o*(cLV + CDSV)                                         (2.34)

           where:
                CF  = Fixed cost if repair is needed [NOK]
                30  = Assumed time from buckle occurs until repair [Days]
                    is done and regular pipe laying is started
                CLV = Daily rate of lay vessel (assumed) = 1.5*106 [NOK]
                C~sv = Daily rate of Diving Support Vessel @SV) (assumed) = 1.25*106 [NOK]
                CTOTAL  = CBA*X + (CP + CP)*M                                 (2.35)

           where:
                      =
                C~TAL Total cost of buckle arrestors, repair pipe and repair [NOK]
                M   = Assumed probability of risk of a propagating buckle during the laying, can be
                    between 0 and 1. It is assumed to be 1 for the first 50 km of the first lay season,
                    after which a probability of 0.05 is assumed until the end of the first lay season.
                    For the second lay season a probability of  1 is assumed since the relative cost of
                    delaying the installation of the riser is large.
                    L
                X=-                                                           (2.36)
                    S
           where:
                X   = Number of buckle arrestors for the pipe length considered
                L   = Pipe length considered [m]


           2.8   References
           1.  ABS  (2000),  “Guide  for  Building  and  Classing  Undersea  Pipelines  and  Risers”,
               American Bureau of Shipping.
           2.  ASME  B31.1,  (1951)  “Code  for  Pressure  Piping”,  American  Society  of  Mechanical
               Engineers.
           3.  ASME B31.3, (1993) “Chemical plant and petroleum refinery piping”, American Society
               of Mechanical Engineers.
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