Page 149 - Electrical Installation in Hazardous Area
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Calculation of release rates and extents  1 15


                  possible using Equation 4.23 (assuming Reo.2 = 15) to determine the pool
                  area and diameter as follows:
                        A = 5.65 x lo2 x 4 x lop5 x  [680 x 2 x 102]0.5 x 15/0.71 x 68   m2

                        A = 81.2 (say 82)                                         m2
                    The figure for Ro.2 at this size of  pool is around 17 and thus the equation
                  should be solved using this figure which will give:-
                                                A = 93                            m2

                    From the normal circular relationship the diameter can be calculated:
                                                d = 11                             m

                    For this part of  the exercise it remains only to calculate the extent of  the
                  hazardous area from the edge of, and above, the pool using Equation 4.26:

                               X = [5.8 x lo-*  x 9.6 x 0.71 x 295/1 x 17]'.14
                               x=9                                                 m

                  Thus there will be, due to the pool and liquid jet, a hazardous area 9 m high
                  for a circle of  radius 26m from a point on the ground vertically below the
                  leak orifice.
                    We now have to consider, in this case because of  the pressure, the possi-
                  bility of  a mist comprising all of  the released liquid being formed at the
                  point of  leakage. To  decide if  this release is diluted by wind action or by
                  its own energy it is necessary to determine the velocity of  the liquid release
                  as this will give an indication of  the effect which the wind  will have on
                  dispersion. The velocity of  release can, as already indicated, be determined
                  by using equation 4.13 but dividing by 01  to convert to volume, and by the
                  orifice area to give velocity. Thus:

                                            Velocity = 13.7                      m/s
                  This is a fairly low velocity and it has to be assumed that the wind will play
                  a large part in dispersion. The hazardous area around the leak orifice has
                  to be assumed to be that which would be produced by total vaporization
                  of  the release diluted by wind action. (Equation 4.7). Thus:
                                      X = 10.8[0.53 x 295/68 x l]o.55              m

                                      X= 17                                        m
                    As the hazardous area touches the ground then this figure needs to be
                  multiplied by 1.5 as previously stated. Thus:
                                                X  = 26                            m
                    The hazardous area produced by this example will therefore be a hori-
                  zontal radius  of  26m  to  a height  of  10m with  a  partial  sphere  above it
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