Petroleum Refining Design and Applications Handbook. A. Kayode Coker

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Petroleum Refining Design and Applications Handbook - A. Kayode Coker

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with Transmitter for recording Flow Controller No. 1 TrRFC-1F, Flow Transmitter for Recording Flow controller No. 1 IPC-8, Indicating Pressure Controller No. 8 IFC-6, Indicating Flow Controller No. 6 IFM-2, Indicating Flow Meter No. 2 RLC-, Recording Level Controller RLM-, Recording Level Meter ILC-, Indicating Level Controller LC-, Level Controller PC-, Pressure Controller

      Control valves carry the same designation as the instrument to which they are connected. Thermocouples carry the same designation as the recorder or indicator to which they are connected. Sequential point numbers are indicated thus (see Table 14.6):

RTM-6-4, Thermocouple connected to point No. 4
RTM instrument No. 6. Also see Figure 14.9.

      Additional symbols include:

PG-6, Pressure Gage No. 6 connected in the field on some item of equipment. If panel board mounted, it becomes-6B.
LTA-1, Low Temperature Alarm No. 1
HTA-1, High Temperature Alarm No. 1
LPA-2, Low Pressure Alarm No. 2
HPA-2, High Pressure Alarm No. 2
LLA-6, Low Level Alarm No. 6
HLA-8, High Level Alarm No. 8
PG-, Push Button

      Process flowsheets do not normally show companion flanges for valves unless these serve as blinds or for orifice plates. This detail is sometimes shown on the piping flowsheet, but here again the use of detail, which does not contribute to the communication function of the sheets, is avoided. Such detail can be time consuming when considered over the entire set of sheets for a process. Figures 14.7 and 14.9 are typical of reasonably good presentation without unnecessary detail. Such specifications as heights of a seal leg, locked open valve, or other information not summarized elsewhere must be recorded on the flowsheets.

      As a direct companion of the completed flowsheet, the line schedule sheet transmits the process and mechanically necessary details for proper interpretation of the piping aspects of the flowsheet (see Figures 14.20ad). These schedules are initiated by the process engineer to further explain the requirements of the process as shown on the flowsheets. They are often and perhaps usually cooperatively completed by other engineers, particularly the piping, mechanical and instrumentation groups.

Modification of ISA Standards
First Letter Second and Third Letters
Controlling Devices Measuring Devices Alarm Devices
* Process Variable or Actuation Recording Indicating Nonindicating (Blind) Valves Self-Actuated valve Safety Valve Recording Indicating Recording Indicating Nonindicating (Blind) Primary Elements Wells Glass Devices for Visual Observation
RC IC C CV V SV R I RA IA A E W G
Flow F FRC FIC FV FR FI FRA FIA FA FE FG
Level L LRC LIC

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