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280                                Well Control for Completions and Interventions


                contraction and ballooning. If the tubing is free to move (seal
                assembly and PBR) the combination of cooling, ballooning, and
                piston force will result in significant upwards movement of the tub-
                ing end, and there is a risk the end of the tubing will pull out of
                the seal bore. If the tubing remains within the seal bore, the
                combination of compressive piston force and high internal pressure
                will promote buckling.
             •  Wellhead and tree pressure working pressure.
             •  Safety valve opening pressure: the control line pressure required to
                keep  a  downhole   safety  valve  open  is  normally  about
                1500 2500 psi (10,000 17,000 kPa) more than tubing pressure.
                Tubing pressure at the beginning of a bullhead may be significantly
                higher than the normal wellhead closed-in pressure. If the well is
                equipped with a tubing retrievable safety valve, control line pres-
                sure will have to be increased to compensate. Failure to do so risks
                damaging the downhole valve. If the well is equipped with a wire-
                line retrievable valve, this can be pulled before the bullhead starts.
          •  Condition of completion:
             •  Tubing burst limits: most operators recommend using 80% of API
                (American Petroleum Institute) burst as an upper limit during a
                bullhead kill. Burst pressures for API pipe grades are readily avail-
                able from tables. If no tables are available, burst can be calculated
                using Barlow’s formula (API values are calculated from Barlow’s
                formula).
                                                2Y p t
                                        P b 5 Tol                      (7.7)
                                                OD
          where:     P b : burst pressure, psi.
                    Tol: API wall thickness tolerance (0.875 for most API grades;
                        0.9 for some cold worked corrosion resistant alloys).
                    Y p : tubing yield, psi.
                     T: tubing wall thickness, in.
                   OD: external diameter of tubing, in.
                   API burst value assumes new undamaged pipe. A lower burst
                value should be used if the pipe has been corroded or worn. API
                burst values should be treated with caution, as they will be altered
                by tri-axial loading during the kill. If the tubing is anchored to the
                packer injection of cold fluid under pressure, this will increase ten-
                sion. Tubing under tension can have a tri-axial burst limit higher
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