Page 450 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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416                       Applied Process Design for Chemical and Petrochemical  Plants





























                                                                 3.  Pressure relief must be adequate  to prevent internal
                                                                   pressures from rising over 10%  above  the maximum
                                                                   allowable  working pressure,  except when  the excess
                                                                   pressure  is  developed  by  external  fire  or  other
                                                                   unforseen  heat  source.  See  design  details  in  later
                                                                   paragraph.  Papa  [85]  proposes  an  improved  tech-
                                                                   nique for relief  sizing. Also see Figures 7-7 A and 7-7B.





                                                                 4. When  a  pressure  vessel  is  exposed  to  external  heat
                                                                   or  fire,  supplemental  pressure  relieving  devices  are
                                                                   required  for  this  excessive  pressure.  These  devices
                                                                   must have  capacity  to  limit the  overpressure  to  not
                                                                   more than 21 % above the maximum allowable work-
                          Assembly  UA-2M                          ing pressure  of the vessel.  (See Figures  7-7 A and  7-
                                                                   7B.) A single relieving device may be used to handle
                                                                   the capacities of paragraph UG-125 of the code, pro-
         Figure 7-SP.  Typical  union type disk holders.  They are not all avail-   vided it meets  the  requirements  of both  conditions
         able.  By permission, B.S.&B.  Safety Systems,  Inc.      described.


             pressure  devices.  There  are  exceptions  covered  by
             paragraph  U-1  of the  code,  and  in  order to omit a
             protective  device  this  paragraph  should  be  exam-   5.  Rupture  disks  may  be  used  to  satisfy  the  require-
             ined  carefully.  For  example,  vessels  designed  for   ments  of the code for conditions  such  as  corrosion
             above 3000 psi are not covered; also vessels with <120   and polymer formations, which might make the safe-
             gallons of water, vessels with inside diameter not over   ty/relief  valve inoperative, or where small leakage by
             6 inches  (at any pressure), vessels having internal or   a safety valve cannot be  tolerated.  They  are particu-
             external  operating  pressures  not  over  15  psig   larly helpful for internal  explosion pressure release.
             (regardless of size), and a few other conditions  may
             not be subject to this code.
                                                                 6.  Liquid  relief valves  should  be  used  for vessels  that
           2.  Unfired steam boilers must be protected.            operate full of liquid.
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