Page 200 - International safety guide for oil tankers and terminals
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INTERNATIONAL SAFETY GUIDE FOR OIL TANKERS AND TERMINALS



                             11.1.7.2     Controlling Electrostatic Generation
      ---ใช้เพื่อการศึกษาเท่านั้น---
                                            Electrostatic discharge has long been known as a hazard
                                            associated with the handling of petroleum products.
               งานห้องสมุด ศูนย์ฝกพาณิชย์นาวี
                                            FAILURE TO FOLLOW THE GUIDANCE GIVEN IN THIS
                                            SECTION WILL LEAD TO THE HAZARDOUS CONDITIONS
                                            REQUIRED FOR ELECTROSTATIC IGNITION ACCIDENTS
                                            TO OCCUR.

                                            When a tank is known to be in an inert condition, no
                                            antistatic precautions are necessary.

                                            If a flammable atmosphere is possible within the tank, then
                                            specific precautions will be required with regard to
                                            maximum flow rates and safe ullaging, sampling and
                                            gauging procedures when handling static accumulator
                                            products.

                                            Mixtures of oil and water constitute a potent source of
                                            static electricity. Extra care should therefore be taken to
                                            prevent excess water and unnecessary mixing.


                                                                          ึ
                             11.1.7.3     During Initial Filling of a Tank

                                          The generally accepted method for controlling electrostatic
                                          generation in the initial stages of loading is to restrict the velocity
                                          of oil entering the tank to 1 metre/second until the tank inlet is
                                          well covered and all splashing and surface turbulence in the tank
                                          has ceased.

                                          The 1 metre/second limit applies in the branch line to each
                                          individual cargo tank and should be determined at the smallest
                                          cross-sectional area including valves or other piping restrictions in
                                          the last section before the tank’s loading inlet.


                                            Minimum Diameter of Piping*        Approx. Flow Rate
                                                                                     3
                                                       (mm)                        (m /hour)
                                                         80                            17
                                                        100                            29
                                                        150                            67
                                                        200                           116
                                                        250                           183
                                                        305                           262
                                                        360                           320
                                                        410                           424
                                                        460                           542
                                                        510                           676
                                                        610                           987
                                                        710                         1,354
                                                        810                         1,782


                                                Table 11.1 – Rates corresponding to 1 metre/second

                                               * Note that the diameters given are nominal diameters, which are not necessarily
                                                           the same as the actual internal diameters.




      166                                      © ICS/OCIMF/IAPH 2006
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