Page 540 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 540

506                       Applied Process Design for Chemical  and Petrochemical  Plants













                                                                                                      _  TYPICAL
                                                                                                        ELBOW MOUNTED
                                                                                                        HAD EXTINGUISHER
                                                                                                        ON DUCT




                                                                                         SAFETY DISCONNECT SWITCH
                                                                                         ON ACCESS HATCH




                                       TYPICAL EXTINGUISHER
                                       MOUNTED ON RAISED
                                       HOUSING (INSTALLER
                                       FABRICATED)









                         Figure 7-62.  Typical  Fenwal explosion suppression system.  By permission,  Fenwal Safety Systems,  Inc.




            relates  to  explosion  prevention systems  and  the  "design,   P;  =  the maximum initial pressure at which the com-
            construction,  operation,  maintenance and testing of sys-      bustible atmosphere exists,  psig
            tems for the prevention of  deflagration explosions" and is   R  =  the ratio of the maximum deflagration pressure  to
            a  valuable  document  for  designers.  One  significant        the maximum initial pressure, as described in
            requirement of this code relates to establishing the design     Code Par 5-3.3.l
            pressure of a ASME code pressure vessel if the vessel is  to   Fu  =  the ratio of the ultimate stress of the vessel  to the
                                                                            allowable stress of the vessel
            possibly  be  subject to  and contain  a deflagration  and  its
            explosion pressure internally:                              F,  =  the ratio of the yield stress of the vessel to the
                                                                            allowable stress of the vessel
                                                                    Note:  1  psi  =  6.89 kPa.
              From  NFPA-69  [55), extracted  by  permission.  Design
            Pressure:                                             5-3.3.1  The dimensionless ratio R is the ratio of the maxi-
                                                                  mum deflagration pressure,  in absolute pressure units,  to
                   1.5[R(P.  +14.7)-14.7]                         the maximum initial pressure,  in consistent absolute pres-
                          I             ,  psig          (7- 64)   sure  units.  For gas/air mixtures,  R shall  be  taken  as  9.0;
                            F  u                                  for dust/air mixtures,  R shall be taken as  10.0.
                   1.5[R(P.  +14.7)-14.7]                         Exception: A different value of R may be used if appropri-
              pd  =       I             >  psig          (7-65)   ate  test data  or calculations  are  available  to  confirm  its
                            FY
                                                                  suitability.
            where  Pr  =  the design pressure  to prevent (vessel)  rupture   5-3.3.2 For operating temperatures below 25°C,  the value
                      due to internal deflagration, psig          of R shall be adjusted according to the following formula:
                  Pd  =  the design pressure to prevent deformation due to
                      internal deflagration, psig                   R' =  R  [298/  (273  + T;)]               (7-66)
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