PIPING & INSTRUMENTATION DIAGRAM.pdf

PIPING
&
INSTRUMENTATION
DIAGRAM
21st
Oct 2015 Presented by : Muhammad Afzal Kayani

Objective
The aim of this course is to develop
a basic understanding of
analyzing/interpreting
P & I Diagrams and its utilization

P & ID
 Introduction
 Skill for Analysis & interpretation of
Process Flow Diagrams
 3 Level of Diagrams
 Introduction to Block Flow Diagram
(BFD)
 Introduction to Process Flow Diagram
(PFD)
 PFD Symbology & Abbreviation
 Introduction to Piping & Instrumentation

P & ID
 P & ID Symbology & Abbreviation
 Introduction to Process Control Loop
 How To Read a P & ID
 Piping Specifications & Decoding
 Interlock System
 Piping Isometrics
 Equipment Elevation Drawings

Introduction
WHY skill is
necessary for
chemical plant
personnel in
analyzing &
interpreting
Process Flow
Diagrams ?

Introduction
 Complex chemical processes
 High temperature, pressure,
energy
 High reactivity & toxicity of
chemicals
 Serious consequences in case of
missed communication
 Appropriate process diagrams are
required for clear visual
information
Flow Diagrams communicate information about a process in
the most effective way.

Introduction
 Block Flow Diagram (BFD)
 Process Flow Diagram (PFD)
 Piping and Instrumentation
Diagram (P&ID) – often referred
to as Mechanical Flow Diagram
3 Levels of Diagram are generally applied in process
industry.

Introduction
Each step shows additional information.

Block Flow Diagram (BFD)
 BFD shows overall processing picture of a chemical complex & is
useful as an orientation tool.
 Chemical process can be broken down into basic areas or blocks.
 Diagram consists of a series of blocks representing different
equipments or unit operations that are connected with input &
output streams.
Air
NH3
Urea Prills
Ammonia
Unit
Urea
Unit
Bagging
&
Shipping
Utility
Unit
Fuel Gas Utility
Unit
Steam
NG
CO2

Block Flow Diagram (BFD)
Following conventions are used,
 Only limited information is available about each process
unit.
 Each block represents a process function which in reality
may consist of several pieces of equipment.
 Major flow lines shown with arrows giving direction of flow.
 Flow goes from left to right whenever possible.
 Light streams (gases, vapors) move towards top and heavy
streams (solid, liquid) go towards bottom.
Diagram is very useful for “getting a feel” for the process & is a
starting point for developing a PFD.

Process Flow Diagram (PFD)
PFD provides basic information of the following,
1. Process fundamental details
2. Process stream Information
3. Equipment information

 Bulk of information about
chemical process is
available as compared to
BFD.
 There are no universally
accepted standards about
contents of information.
 PFD information for same
process may differ from one
company to another
company.

It normally includes,
 All Major Equipments with a
descriptive name & unique
equipment number
 Process condition & chemical
composition of each stream
 Bypass & Re-circulation Streams
 Flow & equipment summary table
 Basic control loops, illustrating the
control strategy used to operate the
process during normal operation
Showing the connectivity & flow relationship between major
equipments of plant

It does not include,
 Minor piping details (Piping line #,
piping class)
 Manual isolation & shut-off valves
 Flanges
 Vents & drains
 Instrumentation
 Safety relief valves
Displays the flow relationship between major equipments of plant

Introduction to Process Flow Diagram
(PFD)
 Computer generated with the
help of process simulators
 CAD Package
 Standard symbols / icons are
used
 Arrows show the flow of
chemicals

 PFD are produced by drafting department working with process
engineering.
 A well-known engineering & construction firm (consultant) may be
hired for above task.
 PFD & PIDs are approved after completion.
 The value of the PFD does not end with the construction of plant.
 It remains the document that best describes the process, and is used in
the training of operators and new engineers.
 It is consulted regularly to diagnose operating problems that arise and to
predict the effects of changes on the process.

Process
Equipment
Identification
T – Turbine
K - Compressor
E - Heat
Exchanger
V - Vessel
P - Pump
R - Reactor
C – Column / Tower
T - Storage Tank
F - Fired Heater
Conventions used for identifying Process Streams &
Equipment
Utility Streams
CW : Cooling Water
NG : Natural Gas
UN : Utility Nitrogen
IA : Instrument Air
HS : High Pressure
Steam
FG : Fuel Gas
DMW : De-mineralized
Water
FW : Fire Water
Process
Streams
PG : Process Gas
AL : Liquid
Ammonia
US : Urea Solution

Equipment Numbering System
P – 101 A/B
Pump
01 Area
Pump # 01
Back up pump is available

Information Flags
 Not all process information is of equal importance.
 Information critical to the safety & operation of the plant
is included.
 This includes temperature pressure & flow rates of feed &
product streams.
 The information provided on the flags is also included in
the flow summary table. Therefore flags are useful in
reducing size of flow summary table.

Information Flags For Stream
Identification
Stream information is added to the diagram by attaching “ information flags”

Piping & Instrumentation Diagram

 Principal or core document in a process industry
 Overall document used to define a process
 Provides information to begin planning for construction of plant
 The P & ID includes every mechanical aspect of the plant except
stream flows, pipe routing, pipe lengths, pipe fittings, supports,
structure & foundations
 Sets of symbols are used to depict mechanical equipment, piping,
piping components, valves, drivers and instrumentation and controls.
 There is no universal, national, international standard that specifies
what information should be included on a P&ID
 Some changes will probably be included when the revision is issued
 Reflect process improvements and additions, as well as changing
Introduction to P & ID

Development of a P & ID
 P & IDs develop in steps
 Lay out a conceptual pass at showing vessels, equipment and
major piping
 The instrumentation and controls are typically added next
 Specialists fill in the information regarding the equipment: size,
rating, throughput, and utility usage (horsepower)
 P & IDs are controlled documents formally issued at various
stages. Control means changes to the drawings are identified
and documented.
 Formal issue process occurs several times in the course of a

Introduction to P & ID
It includes,
 Basic operational & startup
information
 Equipment capacity & rating
 Piping details (Piping line #, piping
class)
 All isolation valves with
identification
 Startup & flushing lines
 Interconnections
 Vents & drains
 Safety relief valves
 Control loops & Instrumentation
 DCS Inputs
Defines a process – Equipment, piping and all monitoring & control components

Piping & Instrumentation Diagram (P &
ID)
 Used for planning & construction of
plant
 Used to operate the process
 Used for maintenance &
modification of process
 Used by mechanical technicians &
safety personal
 Used for HAZOP study of plant
 Controlled document formally
issued at various stages of project

P & ID Symbology & Abbreviation

P & ID Symbols - Abbreviations
PRESSURE
PC = Controller
PI = Indicator
PIC = Indicator-controller
PR = Recorder
TEMPERATURE
TE = Temperature sensing element
Th = Thermometer Indicator
TRC = Recorder-controller
TR = Recorder
LEVEL
LC = Controller
LG = Glass
LI = Indicator
LR = Recorder
FLOW
FC = Controller
FE = Test orifice plate
FI = Indicator
FR = Recorder

P & ID Symbols - Abbreviations
SELF OPERATED
CONTROL VALVES
FCV = Flow
LCV = Level
PCV = Pressure
TCV = Temperature
MISCELLANEOUS
SG = Sight Glass
FV = Straightening Vains
HC = Hand Control
PSD = Pressure Safety Device
PSV = Pressure safety valve

Location Of Instrument
Locally Mounted
Mounted on panel board in control room
Mounted on local panel board
Local Transmitter
Electric – Pneumatic Converter

Process Control Loop
Simple instruments permit direct reading of a process
variable in the field. These devices include pressure
gauges, thermometers, level gauges and rotameters.
Automatic Control Loop
It consists of three parts
 Sensing
 Comparing
 Correcting

In automatic control, the three devices –
the transmitter that senses, the
controller that compares, and the
control valve that corrects – are
interconnected to form a control loop.
The interconnection may be
pneumatic, electronic, digital, or a
combination of all three. The
pneumatic component is typically a
3-15 psig (pounds per square inch
gauge) instrument air signal. If the
interconnection is electronic, a 4-20
mA (mill amperes) signal is usually

Sensing : To measure / sense a process variable
 Flow of fluid in a pipe
 Level of a liquid in a tank
 Temperature of a fluid in a vessel
 Pressure of gas in a pipe
Normally these process variables are measured continuously. A transmitter
measures the process in some way and transmits the information to a central
location (sends an electrical signal) where the comparison takes place. The
central location is usually a control room where plant operators monitor the
process, or, the rack room where the process control computer is located
that performs the comparison.

Process Control Loop: Temperature
Sensing
RTD
Thermocouple

Process Control Loop : Level Sensing
Capacitance Type
Float Type
Differential pressure Type
Bubbler Type
Radar Type
Radioactive

Process Control Loop : Flow Sensing
Magnetic Type
Venturi Type
Orifice Type
Vortex Type
Flow Totalizer

Flow Measurement
Flow Glass Orifice Plate Venturi Tube Pitot Tube
Flow Totalizer Magnetic Flowmeter Vortex Meter

Comparing :
The electronic controller is located in
control room in the console and its
face plate can be observed by the
operator via a shared control
system, such as a distributed control
system (DCS) or a programmable
logic controller (PLC). The value of
the process variable is compared
with the desired value (the set
point), and action is taken to develop
a signal to bring the two together.

Process Control
Correcting :
The control device then develops a signal to bring the
process variable and the set point together. From the
controller an electronic signal is sent to a device (E/P) in
the field that computes the correct valve position & send
a pneumatic signal to activate the final control element.
This device is most often a control valve or a variable
speed pump drive. Control valves usually are
pneumatically actuated, often by a 3-15 psi signal & are
supplied with a positioner to provide feedback of valve
position.
In order to warn operator about potential problems , high &
low level alarms are provided , they receive the same

Final Control Element
Electronic to
Pneumatic Converter Final Control
Element
Control Valve

Control Valve Action
The control action that finally takes place in the field is not
describes explicitly in neither PFD nor P & ID. However is a
simple matter to infer that if there is an increase in level of a
vessel , the control valve will open slightly and the flow of
liquid will increase, tending to lower the level in the vessel.
For a decrease in the level of liquid, the valve will close
slightly.

Control Loop Tuning Parameters
The response time of the system depends upon type of
control action used.
P - Proportional or gain – how far away the process variable
is from the set point
I - Integral or reset – how long the process variable has been
away from the set point
D - Derivative or rate – how fast the process variable is
changing

Control valves may fail in various positions – open, closed,
locked. The position of a failed valve can have a significant
impact on associated equipment, and, therefore, it is of interest
to operations personnel. The fail positions may be identified
on the P&ID using letters below the valve symbol: FO for Fail
Open; FC for Fail Closed; FL for Fail Last or Locked.

Valve type
VS
VD
VR
VB
VDR
VF
VM
VP
Gate Valve
Globe, Needle or Angle Valve
Plug Valve
Ball or 3-way Plug Valve
Check Valve
Butterfly Valve
Diaphragm Valve
Piston Valve

PLUG
BUTTERFLY
Three-way Valve
Four-way Valve
CHECK VALVE

Welded Valve
Flanged Valve

M
M
Diaphragm operated
With Manual Hand wheel
Piston Operated
Solenoid Operated
Motor Operated

Line
Symbols
Instrument Connection to Process
Pneumatic Signal
Electric Signal
Hydraulic Signal
Capillary Tube
Electromagnetic Signal
Software Data Link
Mechanical Link
Line symbols are used to define the ways information
is transferred between the field devices and the
central control location. The symbols describe how
signals are transmitted between devices.

Line Symbols
Hot Insulated Line
Cold Insulated Line
Jacketed Line
Insulated Line with external tracer
Capillary Tube
Electrical Transmission
Pneumatic Transmission
Process piping for Instrument

Piping Specification & Decoding
It provides information about,
 Material of construction
 Design temperature & pressure
 Line size & thickness
 Valves & gaskets compatibility
 Used for any branching (off-take)
R-101 E-101
8˝-41-P28-99A-T

- Just like equipment, pipes on the flow diagram must be
identified
- Pipe line symbol, is used in which to place this information
- In some instances the pipe specification symbol is located
directly in the flow line
- In other instances the specification information is written
above the line
12˝-30-HS33-55A-I
12˝-30-HS33-55A-I

R-101 E-101
8˝- 01- P28 - 99A -T
Line Size
Area Code
Fluid Type
Line No.
Material Snam. Spec
Rating Internal / External
Treatment

12˝-30-HS33-55A-I
V-4301 ME-4302
Line Size
Area Code
Fluid Type Line No.
Snam. Spec.
Coating Designator

System Code
Area Code
01 : Urea
02 : Reforming Section
03 : CO2 absorption Section
04 : Synthesis gas compression
05 : Ammonia Synthesis
06 : Steam Generation
07 : Power Generation
08 : CW circulation

Fluid Type
KS Very High Pressure Steam
HS High Pressure Steam
LS Low Pressure Steam
P Process Fluid
IA Instrument Air
UA Utility Air
UN Utility Nitrogen
12˝-30-HS33-55A-I

Material
1 Carbon Steel
3 Austenitic Stainless Steel
4 Reinforced Thermal Resin Pipe
5 Si Killed Carbon Steel or CrMo steel
6 Ferritic Alloy Steel
7 Cast Steel
8 Austenitic SS or Ferritic Alloy Steel
9 Urea Grade SS
55A

Material Rating
1 150#
3 300#
5 600#
6 900#
7 1500#
8 2500#
9 Special
55A

Insulation Specification
12˝-30-HS33-55A-I
N Not Painted /Insulated
PP Personnel Protected
S Internal Treated/External Painted
A Internal Treated, External coated
B External Coated
E Electric traced
F Cold Insulated
I Hot Insulated
T Steam traced
V External painted
W Jacketed

Ceramic Lined Pipe
Concrete Lined Pipe
A- Internal Treated, External coated
PIPE COATING DESIGNATOR - A

Coating and wrapping for underground
installation
B- External coated
PIPE COATING DESIGNATOR - B

PIPE COATING DESIGNATOR - E
E- Electric Traced

PIPE COATING DESIGNATOR - F
Cold Insulated pipe for low temperature service
F- Cold Insulated

PIPE COATING DESIGNATOR- I
Hot Insulated pipe for High temperature service
I- Hot Insulated

PIPE COATING DESIGNATOR - V
V- External Painted
Painted Pipe

PIPE COATING DESIGNATOR - T
T- Steam Traced

PIPE COATING DESIGNATOR - W
W- Jacketed

Process Conditions
A
B
C
D
A : Operating Temperature (°C)
B : Design Pressure (Mpag)
C :Design Temperature (°C)
D : Full Vacuum

Radial Vibration Interlock system

Axial Vibration Interlock system

Piping Isometrics
 Represents 3D structure of pipe between two points
 Drawn to scale
 All the fittings including, valves, flanges, elbows etc. are clearly
represented
 Detail about bill of material needed for execution of piping
layout
 A table gives the number and detailed description of each type
of fittings
Used for fabrication and then construction of the piping system

Equipment Elevation Drawing
 Shows the vertical location
of process equipment .
 It shows the location of
process equipments in
relation to existing structures
and ground level.
 Useful for performing
startups and shutdowns.

Piping Support Types
Base Support

Variable Spring Support
Beam Support

Anchor Shoes with slide plate
U Clamp Support

Constant Load Hanger
Variable Spring Hanger

PIPING & INSTRUMENTATION DIAGRAM.pdf

PIPING & INSTRUMENTATION DIAGRAM.pdf

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