Page 46 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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Process Planning, Scheduling and Flowsheet Design                       31

                                                       Vessel  and  Tank  Summary
                                                            Mo11riol
                           Equipmul  Type  0.0.  ..   Coi,ocily   Thid:nns.ins.   Cor,o·   Shell  Saddle   Pttnure ,psig   Temp  .•• F.   Refe,ence
                                                   Socldle  1ion
                                      HI.
                     i:,m  No.           Gallons  Shell  Head   Sllirt  Allow,   8   s,irl  Ope,'n.   Dtsi4n  Tut   Optr'n  Oui9n   Codt   Stomp   Drawing   Noles
                                     Lnlh.         Supp 1 f.  ir.chu  Heads  SuPP'I.             Ho.

                                     -        -       -       -                   -  -               --

                                                Figure 1-29. Vessel and tank summary sheet.


                                                       Vessel  and  Tank  Schedule
                       Item   No.   Service  Otscr/pfion   Vertical  or   Olom.  ltn9th   Thictn,11   tinin9   lnaulation   THI   Wtitht   Rtf.  Puchau   P.O.
                       No.   Units          Horizontal       Htad  Shall   Cadt   Pre11utt  I ptiG   Dwt.  Ordtr  To   N••btr





                                                  Figure  1-30. Vessel and tank schedule.



             op  men  t as well as railroads. The checklist of Figure 1-31  is   • ASME Code, Materials Specification, Part B, Non-Fer-
             an example of a helpful form. Others can be developed to   rous Materials
             suit the project or general  plant situation.           • ASME Section V Non-Destruction Examination
               For immediate job  reference  as well  as for estimating   • American  Society  for  Testing  Materials,  Part  10,
             requirements  of a  process  for  expansion  purposes,  the   Annual  Book  of ASTM  Standards:  Metals-Physical,
             form  shown  in  Figure  1-32  is  convenient  and  can  be   Mechanical and Corrosion Testing
             expanded  to suit the process  under consideration.     • General Recommendations for Spacing in Refineries,
                                                                      Petrochemical  Plants, Gasoline Plants, Terminals,
                                                                      Oil  Pump Stations and Offshore Properties,  Industrial
             Standards and Codes
                                                                      Risk Insurance, Hartford, Conn.  (See  [19].)
                                                                     • American Standards Association, Petroleum Refinery
               The  process  design  engineer must in effect become a   Piping ASA B31.3  (latest Edition)
             good general purpose engineer who recognizes the need   • Standards of the Tubular Exchangers  Manufacturers
             for  integrating  the  various  engineering  disciplines  into   Association  (TE.MA Standards,  latest edition)
             the  process  details  as  may  be  required.  The  engineer   • National  Fire  Protection Association as follows:
             becomes  what  might  be  termed  a  pseudo-mechanical,
             corrosion,  and  metallurgical  engineer  as  well  as  a  basic
             chemical  engineer,  The design engineer must,  or should
             soon,  be  knowledgeable  of all  types  of information  and       Standard                        Code
             specifications  necessary  to  totally  perform  the  process   Blower and Exhaust Systems          91
             design  functions  in  all  detail  and  scope.  A  partial  list of   Chemical Reactions,  Hazardous   491M
             these specifications follows.                        Chemical  Data, Hazardous                      49
                                                                  Chimneys, Vents,  Fireplaces,  and
               It is recommended that all pressure vessels and atmos-   Solid Fuel Burning Appliances           211
             pheric  vessels  be  designed,  fabricated,  tested,  and  code   Coding,  Uniform for Fire Protection   901
             stamped according to  the most applicable code as ASME   Dry Chemical Extinguishing Systems         17
             or  API,  regardless  of  service  application  (nuclear  is   Electrical Code, National            70
             excluded from any discussion in these chapters):     Electrical Equipment in Hazardous
                                                                    (Class.)  Locations,  Gases, Vapors,  Dusts   497M
               • American  Society  of Mechanical  Engineers  (ASME)   Electrical Equipment, Purged and
                 Unfired Pressure Vessel Code Section 8, Division 1   Pressurized Enclosures for                496
                                                                  Electrical Installations,
               • ASME  Code, .Materials  Specification, Part A,  Ferrous   Classification of Class  1
                 Materials                                                                             (continued on next page)
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