Page 42 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 42

Process Planning, Scheduling and Flowsheet Design                       29

                                                           Table 1-4
                                  Instrumentation Nomenclature-Complete  General Identification*


                                             MODIFICATION OF  ISA  STANDARDS
                       FIRST  LETTER
                                               Controlling  Devices    Measuring   Alarm
                                                                        Devices
                                                                           I   I
                     * Process
                     Variable
                        or
                     Actuation


                                                                                      IA
                                                                                     -
                                                                                      FIA
           I Level                                                                    LIA
                                                             PV                       PIA






                                                                 ?k?iY?              ~   XIA
                                                              TV                      TIA
                                                                            XI
                                                                               XRA
                                                                       XR
                                                                 XSV
                                                                                     __
           I                    NOTE:  Blank  spaces  are  impossible  or  improbable  combinations.
           By permission, D.J.  Oriolo, 0. & G. Jour., Nov.  17, 1958; Also see ISA Stds. Latest edition.
              Thermocouples  carry  the  same  designation  as  the   sheet, but here again the use of detail which does not con-
           recorder or indicator to which they are connected. Sequen-   tribute  to  the  communication  function  of  the  sheets is
           tial point numbers are indicated thus (see Table 1-4) :   avoided. Such detail can be time consuming when consid-
                                                                 ered over the entire set of sheets for a process. Figures 1-8
              RTM-6-4,   Thermocouple connected to point No. 4   and 1-9 are typical of reasonably good presentation with-
                         RTM instrument No.  6. Also  see Figure   out unnecessary detail. Such specifications as height of a
                          1-10.
                                                                 seal leg, locked open valve, or other information not sum-
              Additional symbols include:                        marized elsewhere must be recorded on the flowsheets.
               PG--6,  Pressure Gage No. 6 connected in the field
                       on some item of  equipment. If  panel board
                      mounted, it becomes-6B.                    Working Schedules
              LTA-1,  Low Temperature Alarm No. 1
              HTA--1,  High Temperature Allarm No. 1
              LPA-2,  Low Pressure Alarm No. 2                     As a direct companion of the completed flowsheet, the
              HPA--2,  High Pressure Alarm No. 2                 line schedule  sheet transmits the  process and mechani-
              EM--6,  Low Level Alarm No. 6                      cally necessary  details for  proper  interpretation  of  the
                  -8,  High Level Marm No. 8                     piping aspects of the flowsheet (see Figures 1-24A, B, C,
               PC-   , Push E1utton                              D) . These schedules are initiated by the process engineer
                                                                 to  further  explain  the  requiremlents of  the  process  as
              Process flowshects do not normally show companion   shown on the flowsheets. They are often and perhaps usu-
           flanges for valves unless these serve as blinds or for orifice   ally cooperatively completed by other engineers, particu-
           plates. This detail is sometimes shown on the piping flow-   larly the piping, mechanical and instrumentation groups.
   37   38   39   40   41   42   43   44   45   46   47