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INTERNATIONAL SAFETY GUIDE FOR OIL TANKERS AND TERMINALS



                                    straight pipe that will expand considerably under thermal loads. The
                                    restraints must both allow for this thermal expansion and absorb the
      ---ใช้เพื่อการศึกษาเท่านั้น---
                                    surge forces without overstressing the pipe.


                                    Where motorised valves are installed, several steps can be taken toชย์นาวี
               16.10 Reduction of Pressure Surge Hazard


                         16.10.1 General Precautions

                                    If, as a result of the calculations summarised in Section 16.9, it is found
                                    that the potential total pressure exceeds or is close to the strength of any
                                    part of the pipeline system, it is advisable to obtain expert advice. Where
                                    manually operated valves are used, good operating procedures should
                                    avoid pressure surge problems. It is important that a valve at the end of a
                                    long pipeline should not be closed suddenly against the flow and all
               งานห้องสมุด ศูนย์ฝกพาณิ
                                    changes in valve settings should be made slowly.


                                    alleviate the problem:
                                      Reduce the linear flow rate, i.e. the rate of transfer of cargo, to a value
                                       that makes the likely surge pressure tolerable.
                                      Increase the effective valve closure time. In very general terms, total
                                       closure times should be of the order of 30 seconds, and preferably
                                                                          ึ
                                       more. Valve closure rates should be steady and reproducible, although
                                       this may be difficult to achieve if spring return valves or actuators are
                                       needed to ensure that valves fail safe to the closed position. A more
                                       uniform reduction of flow may be achieved by careful attention to valve
                                       port design, or by the use of a valve actuator that gives a very slow
                                       rate of closure over, say, the final 15% of the port closure.
                                      Use a pressure relief system, surge tanks or similar devices to absorb
                                       the effects of the surge sufficiently quickly.



                         16.10.2 Limitation of Flow Rate to Avoid the Risk of a
                                    Damaging Pressure Surge
                                    In the operational context, pipeline length and, very often, valve closure
                                    times are fixed and the only practical precaution against the
                                    consequences of an inadvertent rapid closure is correct operation of the
                                    valves and/or to limit the linear flow rate of the oil to a maximum value
                                    related to the maximum tolerable surge pressure.




               16.11 Pipeline Flow Control as a Static Precaution

                         16.11.1 General

                                    Safety procedures for the transfer of static accumulator cargoes require
                                    the linear flow rates of the cargo within the loading lines, both ashore and
                                    on board, to be managed to avoid the generation of static charges during
                                    the cargo transfer (see Chapter 3).












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