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Abbreviations for Use on P&IDs

1. PURPOSE

1.1 This engineering standard defines a common system of terminology and abbreviations to clearly and accurately communicate engineering information on project flowsheets (F/S) and/or piping and instrumentation diagrams (P&IDs).

2. Scope

2.1 This standard applies to all project flowsheets/P&IDs unless otherwise required by a customer.

2.2 Refer to the ASHRAE and BSI information sources, listed in Section 3, for Standard (SI) Units of Measure.

3. RELATED DOCUMENTS

3.1 Air Products Engineering Documents 3SEF0011 Fluid Codes for Use on P&IDs

3.2 American Society of Heating, Refrigeration and Air-Conditioning Engineers, Inc. (ASHRAE) 1993 ASHRAE Handbook Fundamentals I-P Edition

3.3 British Standards Institution (BSI) BS ISO 80000-1 Quantities and Units – Part 1:  General

3.4 The above listed documents are referenced herein and shall apply as specifically designated. Latest edition and addenda in effect shall apply.

4. GENERAL

4.1 Terms that may be abbreviated on project flowsheets/P&IDs are listed in Table 1.

4.2 Abbreviations that may be used on project flowsheets/P&IDs are listed in Table 2.

4.3  Letters are sometimes used to form parts of some other symbols, as in the case of instrumentation. These letters are not considered abbreviations and are not identified in this standard. Refer to a standard ANSI/ISA or DIN flowsheet legend to determine the meanings of symbols.

4.4 Refer to 3SEF0011 for fluid/service abbreviations.

4.5 Unless otherwise indicated, the same abbreviation shall be used for all tenses, for participle endings, for the possessive case, for singular and plural, and for the noun and the modifying forms of a term.

4.6 An abbreviation of a word combination shall not be separated for use individually. For example, the abbreviation FH (flexible hose) shall not be split to use F for flexible and H for hose.

4.7 Abbreviations listed in this standard may be used on project flowsheets/P&IDs with or without explanation.

4.8 Abbreviations that are not listed in this standard may only be used if their meanings are given in a legend that is included on the project flowsheet/P&ID. If this new abbreviation needs to be part of this standard, contact the owner of this standard for approval. 

Table 1 Terms and Their Abbreviations

                     Term Abbreviation
Aboveground AG
Bottom Dead Center BDC
Bottom of Line BOL
Bubble Diagram BBD
Building BLDG
Burner Management System BMS
Calorimeter CAL
Car Seal Closed CSC
Car Seal Open CSO
Cathode Ray Tube CRT
Central Plant Monitoring CPM
Central Processing Unit CPU
Close CLS
Closed CLD
Cold Box CB
Column Can COL CAN
Compander COMPDR
Compressor COMPR
Computer COMP
Computer Automatic Manual Station CA/M
Computer Manual Station CM
Crossover XOVER
Crude Argon CAR
Current To Pneumatic Transducer I/P
Defrost DF
Distributed Control System DCS
Drain D
Duplex Temperature Element DTE
Electric Trace TEL
Electrical EL
Enclosure ENCL
Expansion Joint EJ
Fail Closed FC
Fail Last FL
Fail Open FO
Field FLD
Flexible Hose FH
Flowsheet F/S
Foundation Fieldbus FF
Full Port FP
Function Block Diagram FBD
Gaseous Argon GAR
Gaseous Nitrogen GAN
Gaseous Oxygen GOX
Heater HTR
Helium Rejection Unit HRU
High Point HPT
High Pressure HP

 Table 1 (continued)

Term Abbreviation
Inside I/S
Inside Battery Limits ISBL
Inside Cold Box ISCB
Inside Diameter ID
Inspection Port IP
Instrument Air Supply IAS
Instrument Control Tubing ICT
Insulated INS
Interlock Close ILC
Interlock Logic Diagram ILD
Interlock Open ILO
Liquid Argon LAR
Liquid Helium LHe
Liquid Hydrogen LH2
Liquid Nitrogen LIN
Liquid Oxygen LOX
Load Relay LR
Lock Closed LC
Lock Open LO
Low Point LPT
Low Pressure LP
Low Temperature Diode LTD
Lower Explosive Limit LEL
Main Air Compressor MAC
Maintain De-energized DE-EN
Maintain Energized EN
Malfunction MALF
Manhole MH
Medium Pressure MP
Millivolt to Current Transducer E/I
Momentary Start Signal MST
Momentary Stop Signal MSP
Motor Control Center MCC
Motor Operated Valve MOV
Nitrogen Rejection Unit NRU
Normally Closed NC
Normally Open NO
Open OP
Opened OPD
Operator Interface Unit OIU
Ortho/Para O/P
Outside O/S
Outside Battery Limits OSBL
Outside Cold Box OSCB
Outside Diameter OD

Table 1 (continued) 

Term Abbreviation
Piping and Instrumentation Diagram P&ID
Process Flow Diagram PFD
Pneumatic PNEU
Pneumatic To Current Transducer P/I
Pressure PRESS
Pressure Tap PT
Process Control Unit PCU
Programmable Logic Controller PLC
Pure Argon PAR
Pushbutton PB
Removable Spool RS
Resistance Temperature Detector RTD
Sample Point SPT
Sanitary Sewer SS
Seal Boot SB
Selective Catalytic Reduction SCR
Side of Line SOL
Sight Glass SG
Start ST
Steam Methane Reforming SMR
Steam Trace STC
Stopped (Not Operating) STP
Storage STOR
Strainer STR
Strainer (Y-Type) STY
Tank TK
Temperature TEMP
Thousand M
Tight Shutoff TSO
Top Dead Center TDC
Top of Line TOL
Top of Pipe TOP
Transition TRANS
Transition Joint TJ
Trap TP
Underground UG
Unspecified Size UNS
Upper Explosive Limit UEL
Utility Connection UC
Vacuum VAC
Vent to Safe Location VSL
Vessel Trim VT

Table 2 Abbreviations and Their Terms

Abbreviation Term
AG Aboveground
BDC Bottom Dead Center
BLDG Building
BOL Bottom of Line
CA/M Computer Automatic Manual Station
CAL Calorimeter
CAR Crude Argon
CB Cold Box
CLD Closed
CLS Close
CM Computer Manual Station
COL CAN Column Can
COMP Computer
COMPDR Compander
COMPR Compressor
CPM Central Plant Monitoring
CPU Central Processing Unit
CRT Cathode Ray Tube
CSC Car Seal  Closed
CSO Car Seal Open
D Drain
DCS Distributed Control System
DE-EN Maintain De-energized
DF Defrost
DTE Duplex Temperature Element
E/I Millivolt To Current Transducer
EJ Expansion Joint
EL Electrical
EN Maintain Energized
ENCL Enclosure
FBD Function Block Diagram
FC Fail Closed
FF Foundation Fieldbus
FH Flexible Hose
FL Fail Last
FLD Field
FO Fail Open
FP Full Port
F/S Flowsheet
GAN Gaseous Nitrogen
GAR Gaseous Argon
GOX Gaseous Oxygen
HP High Pressure
HPT High Point
HRU Helium Rejection Unit
HTR Heater

Table 2 (continued) 

Abbreviation Term
IAS Instrument Air Supply
ID Inside Diameter
ILC Interlock Close
ILD Interlock Logic Diagram
ILO Interlock Open
INS Insulated
IP Inspection Port
I/P Current To Pneumatic Transducer
I/S Inside
ISBL Inside Battery Limits
ISCB Inside Cold Box
LAR Liquid Argon
LC Lock Closed
LEL Lower Explosive Limit
LH2 Liquid Hydrogen
LHe Liquid Helium
LIN Liquid Nitrogen
LO Lock Open
LOX Liquid Oxygen
LP Low Pressure
LPT Low Point
LR Load Relay
LTD Low Temperature Diode
M Thousand
MAC Main Air Compressor
MALF Malfunction
MCC Motor Control Center
MH Manhole
MOV Motor Operated Valve
MP Medium Pressure
MSP Momentary Stop Signal
MST Momentary Start Signal
NC Normally Closed
NO Normally Open
NRU Nitrogen Rejection Unit
O/P Ortho/Para
OD Outside Diameter
OIU Operator Interface Unit
OP Open
OPD Opened
O/S Outside
OSBL Outside Battery Limits
OSCB Outside Cold Box
PAR Pure Argon
P&ID Piping and Instrumentation Diagram
P/I Pneumatic To Current Transducer
PB Pushbutton
PCU Process Control Unit
PFD Process Flow Diagram
PLC Programmable Logic Controller

Table 2 (continued) 

Abbreviation Term
PNEU Pneumatic
PRESS Pressure
PST Permit Start
PT Pressure Tap
RS Removable Spool
RTD Resistance Temperature Detector
SB Seal Boot
SCR Selective Catalytic Reduction
SG Sight Glass
SMR Steam Methane Reforming
SOL Side of Line
SPT Sample Point
SS Sanitary Sewer
ST Start
STC Steam Trace
STP Stopped (Not Operating)
STOR Storage
STR Strainer
STY Strainer (Y-Type)
TDC Top Dead Center
TEL Electric Trace
TEMP Temperature
TJ Transition Joint
TK Tank
TOL Top of Line
TOP Top of Pipe
TP Trap
TRANS Transition
TS To Stack
TSO Tight Shutoff
UC Utility Connection
UEL Upper Explosive Limit
UG Underground
UNS Unspecified Size
VAC Vacuum
VSL Vent to Safe Location
VT Vessel Trim
XOVER Crossover

 

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