Page 99 - Electrical Installation in Hazardous Area
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Area classification for gases, vapours and mists  75


                   to limit the Zone 1 produced to a distance of  1.5m above and around the
                   flexible coupling projected vertically down to the ground.
                     Zone 2  This will result due to abnormal circumstances, the first of  which
                   will occur if the tanker is overfilled. In these circumstances the liquid will,
                   as in the case of  a fixed tank, flow out of  the vents and down the sides of
                   the tank, ultimately forming a pool on the ground. The Zone 2 produced
                   above and around the tank by this event will be no larger than the Zone 1
                   produced by vapour release and the resulting Zone 2 will be invisible in
                   the case of  the loading of  road/rail  tankers but, as it is due to abnormal
                   circumstances, it cannot be presumed not to exist in the unloading scenario.
                   Therefore a 1.5m Zone 2 above and around the tank will be present in all
                   circumstances and will be projected vertically down to  the  ground. The
                   pool of  flammable liquid formed on the ground will grow until it is either
                   contained or until its vaporization rate is equal to the release rate of  liquid
                   from the tank (see Chapter 4). The hazardous area created by this pool will
                   be Zone 2 and will be sized as given in Table 3.7.
                     A  second  source  of  release  in  abnormal  circumstances will  be  that
                   occurring  when  a  flexible  connecting  pipe  actually  ruptures.  In  this
                   circumstance it is not expected that total rupture will take place due to the
                   sort of  reinforcement provided in such connecting pipes and, therefore, a
                   similar release to that occurring with rupture of  a CAF gasket is considered
                   to be a fair model. Again, the release of  liquid will form a pool and the
                   dimensions of  this pool can be determined from Table 3.3. The extent of  the
                   hazardous area around the pool so formed can then be determined from
                   Table 3.7. As the pressure will be low in these cases it is unlikely that any
                   mist will form and the Zone 2 around the connecting pipe will be minimal.
                   This is academic as a Zone 1 of  1.5m has already been declared and this
                   will encompass any small Zone 2 around the connecting pipe.
                     Finally, it is highly unlikely that solar gain will occur in road/rail tankers
                   unless they are parked for long periods in direct sunlight immediately prior
                   to unloading. Provided care is taken in this regard only liquids with flash-
                   points below 32 "C need be considered.



                   Road or rail tankers containing gases under pressure or
                   liquefied gases and vapours

                   Road  or  rail tankers which contain gases or  vapours under  pressure,  or
                   liquefied gases or  vapours which will  of  course be  also under  pressure,
                   will behave as any other vessel in such circumstances. The mechanisms of
                   release will be principally as follows: liquid, gas or vapour leakages due
                   to coupling and uncoupling; liquid, gas or vapour leakages due to failure
                   of  valve actuator failure; liquid, gas or vapour leakages due to failure of
                   fixed pipe joints; and liquid, gas or vapour leakage due to failure of  flexible
                   couplings.
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