Page 129 - International safety guide for oil tankers and terminals
P. 129

SHIPBOARD SYSTEMS



                                        action to be taken in the event of failure of the inert gas plant during
                                        discharge from inerted tanks, see Section 7.1.12.
      ---ใช้เพื่อการศึกษาเท่านั้น---
                                        If hand dipping of a tank is necessary, pressure may be reduced while
                                        dipping ports are open, but care must be taken not to allow a vacuum to
                                        prevent ingress of air. Whenever pressure falls to the low pressure alarm์นาวี
                                        develop since this would pull air into the tank. To prevent this, it may be
                                        necessary to reduce the cargo pumping rate, and discharge should be
                                        stopped immediately if there is a danger of the tanks coming under
                                        vacuum.

                              7.1.6.7 Ballast Passage
               งานห้องสมุด ศูนย์ฝกพาณิชย
                                        During a ballast passage, cargo tanks other than those required to be gas
                                        free should remain in the inert condition and under positive pressure to

                                        level, the inert gas plant should be restarted to restore the pressure, with
                                        due attention being paid to the oxygen content of the inert gas delivered.

                              7.1.6.8 Static Electricity Precautions

                                        In normal operations, the presence of inert gas prevents the existence of
                                        flammable gas mixtures inside cargo tanks. Hazards due to static
                                        electricity may arise however, mainly in the case of a failure of the inert
                                        gas system. To avoid these hazards, the following procedures are
                                                                          ึ
                                        recommended:
                                          If the inert gas plant breaks down during discharge, operations should
                                           be suspended (see Section 7.1.12). If air has entered the tank, no
                                           dipping, ullaging, sampling or other equipment should be introduced
                                           into the tank until at least 30 minutes have elapsed since the injection
                                           of inert gas ceased. After this period, equipment may be introduced
                                           provided that all metallic components are securely earthed. This
                                           requirement for earthing should be applied until a period of five hours
                                           has elapsed since the injection of inert gas ceased.
                                          During any necessary re-inerting of a tank following a failure and
                                           repair of the inert gas system, or during initial inerting of a non-gas
                                           free tank, no dipping, ullaging, sampling or other equipment should be
                                           inserted until the tank is in an inert condition, as established by
                                           monitoring the gas vented from the tank being inerted. However,
                                           should it be necessary to introduce a gas sampling system into the
                                           tank to establish its condition, at least 30 minutes should elapse after
                                           stopping the injection of inert gas before inserting the sampling
                                           system. Metallic components of the sampling system should be
                                           electrically continuous and securely earthed. (See also Chapter 3 and
                                           Section 11.8.)

                              7.1.6.9 Tank Washing, Including Crude Oil Washing

                                        Before each tank is washed, the oxygen content must be determined,
                                        both at a point 1 metre below the deck and at the middle level of the
                                        ullage space. At neither of these locations should the oxygen content
                                        exceed 8% by volume. Where tanks have a complete or partial swash
                                        bulkhead, the measurement should be taken from similar levels in each
                                        section of the tank. The oxygen content and pressure of the inert gas
                                        being delivered during the washing process should be continuously
                                        recorded.

                                        If, during washing, the oxygen content in the tank exceeds 8% by volume
                                        or the pressure of the atmosphere in the tanks is no longer positive,




                                                   © ICS/OCIMF/IAPH 2006                                        95
   124   125   126   127   128   129   130   131   132   133   134