Primary isolation valves shall be
shown on the P&ID and identified in accordance with valve identification
number. Isolation valves shall be provided for all instrument connections,
isolation of equipment that can be serviced when bypassed, multiple (spare)
pump installations, etc.
The valve type shall be in
accordance with each specific piping material class specification no. Valves
description will as given in the valves specification no. All valves shall be furnished with manual
operators unless specified otherwise.
Gear Operators, as furnished by
the valve manufacturer, shall be provided for large valves which satisfy both
of the following conditions:
Class 150 rating
|
10” size and larger
|
Class 300 rating
|
8” size and larger
|
Class 600 & 900 rating
|
6” size and larger
|
Class 1500 & 2500 rating
|
4” size and larger
|
Gear operators
shall be sized such that its output torque is at least 1.5 times the maximum
required operating torque of the valve proper and shall be suitable for
operation in a tropical environment. The
gear ratio shall be maximum 1:60 for valves NPS 8 and smaller or maximum 1:120
for valve NPS 10 and larger. Gear
operators shall be self locking and be provided with a position indicator.
All valves shall be capable of
being locked in the open or closed position with a positive position locking
device other than chain.
Block valves shall in general be
ball valves of fire safe design in accordance with API 607/API 6FA or
equivalent and a copy of the certification shall be provided. Butterfly valves
may be used in cooling water services. Globe valves will be used when
throttling is required.
Valves shall be provided with
pressure equalizing bypasses when high differential pressure exists across the
closed valve. Valves for which bypasses are to be furnished and the size and
type of bypass valve will be shown on the applicable flow diagram.
All 2” size and larger valves
shall have flanged ends. 1½” and smaller size valves shall have flanged or
socket weld ends.
Check valves will be provided for
all lines tying into common headers, or to prevent back flow.
Flanged end valves which are
described as outside screw and yoke (OS&Y) in the valve classification
tables shall be provided with stem protectors.
Globe, ball, check, and slab-type
gate valves shall be field repairable. Balls, seals and seats shall be replaceable
without welding or cutting.
Valve dimensions shall be
identical to the dimensions specified in ASME B16.10, Face-to Face and End-to-End
Dimensions of Ferrous Valves.
Face-to-face dimensions shall be long patterns.
All valves except check valves
shall be capable of sealing with design pressure applied from either end of the
valve.
Unless otherwise specified,
valves shall be suitable for oil, water, and gas service throughout the
temperature range of the pressure class.
Double seated valves capable of sealing
simultaneously against pressure differential from the bonnet section to the
adjacent pipe in both directions shall be equipped with self relieving
seals. Valves ANSI Class 900 and above
shall have ring joint faced flanges in accordance with ASME B16.20 Ring-Joint
Gaskets and Grooves for Steel Pipe Flanges unless otherwise indicated.
Vent and drain valves shall
comply with the requirements of the valve classification tables and shall be
adequate for the pressure and temperature limits indicated on the material and
service classification data sheets.
Valve pressure-class ratings
shall be in accordance with ASME 16.5.
For testing of valves, API
standard 598, Valve Inspection and Test, or API specification 6D, Pipeline
Valves, shall be used as a basis.
Unless otherwise specified on the
piping material classification data sheets, gate valves shall be outside screw
and yoke (OS&Y) with a rising stem, a bolted bonnet, a bolted packing
gland, and a solid wedge gate.
If resilient seat inserts are
used, the inserts shall be capable of withstanding the maximum temperature
encountered in the service application.
Teflon or reinforced Teflon seat insert is preferred.
Valve seats and seals in service
ASME Class 900 rating and above shall be specified explosive decompression
resistant.
In general reduced bore isolation
valves shall be used in all except the following circumstances:
a.
Manifold valves.
b.
Piggable lines.
c.
Pump suctions.
d.
On drain lines subject to potential blockage.
e. Where
the bore velocity would cause unacceptable pressure loss, noise, erosion, or
exceed supplied specified limits for corrosion inhibitor film stability
The valve stem shall not be
retained by the packing gland. A
shouldered stem with bottom entry is preferred.
The sealing characteristics of
ball valves shall not be impaired by rapid temperature changes or in throttling
application.
The following restrictions apply
to ball valves installed by socket welding or seal welding:
a.
Installation of ball valves by socket welding,
seal welding and stress relieving shall not damage the valve seats.
b.
For all socket weld valves disassembly during
the installation will be required.
Check valves other than the check
valves listed in the piping material classification data sheets may be required
for certain service conditions as given below.
Piping Sizes
|
Check Valves
|
2 Inches and smaller
|
Lift type (ball, piston or disc)
|
3 Inches and larger
|
Spring actuated, double flapper type
|
a.
In services with fluids moving at high
velocities or with pulsating vapour flows, piston check valves shall be used.
b. In
severe service applications, non-slam check valves with hydraulic (or another
type) damping devices shall be used. Lines 8 inches and larger in services that
do not require non-slam devices may use spring-actuated double-flapper type
check valves.
c. Centrifugal
pump discharge check valves shall be of either the lift disc; balanced
tilting-disc or spring actuated double-flapper type
Check valves shall be provided
with drains on the downstream side of the check if required for safe operation
and maintenance.
Wafer type check valves may be
used as an option to flanged swing check valves in ANSI Class 600 and
lower. Wafer check valves shall be
designed to API Std 594, Wafer and Wafer-Lug Check Valves.
Butterfly valves shall be limited
to water and air service. Wafer lug and
wafer drop-in type butterfly valves shall normally be used. Butterfly valves shall be designed to API Std
609, Lug and Wafer Type Butterfly Valves.
A gas safety valve is an important device used to prevent the escape of gas from a pipeline or container. It works by automatically shutting off the flow of gas when it detects a potentially dangerous situation.
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ReplyDeleteProviding good information about butterfly valve.. Really Good. Keep it up.
A butterfly valve is a type of quarter-turn valve that is used to regulate or isolate the flow of fluid in a pipeline.
Petroleum plant design is a complex yet fascinating process that combines engineering expertise, safety standards, and efficiency to create facilities capable of processing crude oil into valuable products. From conceptual planning to detailed design, every element — including piping systems, storage tanks, and safety measures — is meticulously planned to optimize operations. Modern designs focus not only on maximizing output but also on sustainability, reducing environmental impact, and ensuring worker safety.
ReplyDeleteThanks for sharing this topics which covers the diverse range of valves used in piping systems, each tailored for specific functions like flow control, isolation, or pressure regulation, ensuring efficient and safe operations.
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