Page 155 - Electrical Installation in Hazardous Area
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Calculation of  release rates and extents  121


                    The remaining liquid is assumed to reach the ground and the point at
                  which it does is calculated as for liquids below their boiling points, using
                  Equations 4.15 or 4.16 as appropriate.
                    Vaporization is expected immediately contact is made with the ground
                  and the extent of  the hazardous area is calculated as for gas/vapour  using
                  Equation 4.7  with the result multiplied by 1.5 because of  ground proximity.
                    The  hazardous  areas are thus around  the  leak  due  to  vaporization at
                  the leak, and at ground level with an extent from the leak of  the distance
                  travelled by the jet plus the radius of  the area created by vaporization at
                  ground level. The height of  this will be the radius created by ground level
                  vaporization.



                  4.5  Releases in areas which are not well ventilated

                  All of  the foregoing calculations depend  upon wind reaching all parts at
                  around 2m/s. In poorly ventilated areas, such as indoors, this wind does
                  not exist in the same form and is replaced by artificial ventilation in most
                  circumstances. In  addition, the  enclosed  volume  inside the  containment
                  which  limits  the  natural  ventilation  is  not  unlimited.  Thus  all  of  the
                  foregoing calculations must be considered suspect unless the ventilation in
                  all nooks and  crannies of  the enclosure can be  considered as equivalent
                  to  natural  ventilation. In  BS/EN  60079-lo3 which will  replace BS  5345*
                  there is an attempt to define more globally the extents of  and persistence
                  of  explosive atmospheres in a  more general set of  circumstances and the
                  following equations are based upon that.
                    In general, therefore, the only way to deal with indoor areas is to install
                  ventilation taking account of  the leaks present. The minimum flow of  air
                  to dilute a given release of  flammable material to below its lower explosive
                  limit is as follows:

                           Q, = 0.12 x Gf x Tt/To x M x LEL       m3/s (Equation 4.31)

                  This simplifies to:
                                       Q, = 0.03 x Gf x T:/M  x LEL              m3/s

                    where  Q,  = theoretical minimum air flowrate required      m3/s
                             Gf = maximum mass release rate of  flammable material   kg/s
                             T,  = ambient temperature                              K
                             M = molecular weight of  flammable material
                           LEL = lower explosive limit                         % v/v

                  If  Q,  can be related  to the number  of  air  changes around  the source of
                  release (i.e., the airflow velocity) then a further calculation can be carried
                  out to determine the size of  the explosive atmosphere around the gas cloud
                  as follows:
                                               Vm = Qa/C                           m3
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