Saes L 108
Saes L 108
SAES-L-108
Selection of Valves
Document Responsibility: Valves Standards Committee
Contents
Summary of Changes ................................................................................................................................... 3
1 Scope ..................................................................................................................................................... 6
2 Conflicts and Deviations ........................................................................................................................ 6
3 References ............................................................................................................................................. 6
4 General .................................................................................................................................................. 8
5 General Design Limitations .................................................................................................................. 10
5.1 Bonnet/Cover ................................................................................................................................ 10
5.2 End Connections .......................................................................................................................... 11
5.3 Ratings .......................................................................................................................................... 11
5.4 Sizes ............................................................................................................................................. 12
5.5 Stem Packing................................................................................................................................ 12
5.6 Operator ........................................................................................................................................ 12
5.7 Installation ..................................................................................................................................... 12
6 Specific Valve Type Limitations ........................................................................................................... 13
6.1 Ball and Plug Valves ..................................................................................................................... 13
6.2 Butterfly Valves ............................................................................................................................. 13
6.3 Check Valves ................................................................................................................................ 14
6.4 Plug Valves ................................................................................................................................... 15
6.5 Gate Valves .................................................................................................................................. 15
6.6 Manual globe valves ..................................................................................................................... 15
6.7 Chokes .......................................................................................................................................... 15
7 Specific Service Limitations ................................................................................................................. 16
7.1 Low Temperature Services ........................................................................................................... 16
7.2 Underwater Valves ....................................................................................................................... 16
7.3 Pressure Relief Valve Piping ........................................................................................................ 16
7.4 Flare Systems ............................................................................................................................... 16
7.5 Emergency Isolation Valves ......................................................................................................... 16
7.6 Firewater Systems ........................................................................................................................ 17
7.7 Drains and Vents .......................................................................................................................... 17
7.8 Storage Tanks and Vessels .......................................................................................................... 17
7.9 Scraper Trap Valves ..................................................................................................................... 17
7.10 Instrumentation Root Isolation Valves .......................................................................................... 17
7.11 Steam Service .............................................................................................................................. 18
7.12 Blowdown Valves .......................................................................................................................... 18
7.13 Bypass/Equalization Valves ......................................................................................................... 18
7.14 Buried Valves ................................................................................................................................ 18
7.15 Auto-Ignition services ................................................................................................................... 18
7.16 Sectionalizing and lateral valves for pipelines .............................................................................. 19
8 Materials Limitations ............................................................................................................................ 19
Document History ........................................................................................................................................ 19
Materials Appendix ...................................................................................................................................... 20
Summary of Changes
Paragraph Number
Change
Previous Current Technical Change(s)
Type
Revision Revision
07 May 2019 16 Feb 2022
Added SAES-A-134. Updated title for 04-SAMSS-001, 047, 051, and 055.
3 3 Modification Updated description for API 6D and API 6FA. Added API 6A and removed ISO
10423. Added API RP 615 and NACE MR0103/ISO 17945.
Replaced “All requisitions, except those for ISO 10423 valves and chokes, shall
reference 04-SAMSS-035 and 04-SAMSS-048.” with “All requisitions, except
4.5 and 7.9 4.5 Modification those for API 6A valves and chokes, shall reference 04-SAMSS-035 and 04-
SAMSS-048. All requisitions for API 6A valves and chokes shall reference 04-
SAMSS-055.”
Added note “For project reviews, list all Valve Data Sheets for 04-SAMSS valves
4.6 4.6 Modification
and chokes under Index L.”
4.7.1 4.7.3 Editorial Renumbered 4.7.1 as 4.7.3. Renumbered other sections accordingly.
4.7.2 4.7.1 Editorial Added note and included additional definition for proponent in parenthesis.
valves shall not be used as the first block valve against storage tanks or vessels
containing hydrocarbons or hazardous materials”.
7.9 4.5 Modification Removed section covering ISO 10423 valves and chokes. Now covered by 4.5.
Changed “Scraper trap mainline isolation valves shall be full bore through
conduit gate or ball valves in accordance with API SPEC 6D. The seating
configuration shall provide DIB-2 functionality unless otherwise specified. Other
valve types are permitted subject to the review and approval by the Chairman of
7.10.1 7.9.1 Modification the Valves Standards Committee and the Proponent Operating Department on a
case-by-case basis.” to “Scraper trap mainline isolation valves shall be full bore
through conduit gate or ball valves in accordance with API SPEC 6D. The
seating configuration shall provide DIB-2 functionality unless otherwise approved
by the Proponent (Operating organization) on a case-by-case basis.”
7.10.2 7.9.2 Editorial Renumbered paragraph.
Listing the requirement as an exception under 7.10.3. changed reference to ISO
7.10.5 7.9.3 Modification
10423 to API SPEC 6A.
Changed “The scraper trap isolation valve and the kicker valve shall have a
minimum trim metallurgy of Stainless Steel F51, for sour service the minimum
trim metallurgy shall be Alloy 625 or Alloy 718. In addition, the valve seat pockets
(applicable to spring loaded seats only) shall be specified to have an Alloy 625
7.10.4 7.9.4 Modification
weld overlay.” to “Scraper trap isolation valves and kicker valves shall have: (a) a
minimum trim metallurgy of 22Cr Duplex Stainless Steel (UNS S31803); and, (b)
the valve seat pockets for spring loaded seat designs only shall be specified to
have an Alloy 625 weld overlay.”
Removed “Approval of equivalents shall be referred to the Chairman of the
7.11.1 7.10.1 Modification Valves Standards Committee”. Added exception “modular piping class valve
assemblies in 7.11.2 are an exception”.
Removed “subject to specific review and approval by the Chairman of the Valves
7.11.2 7.10.2 Modification Standards Committee on a case-by-case basis”. Added considerations and
criteria for evaluation and use of such valve assemblies.
Removed “Other gate type shall be specifically approved by the Chairman of the
7.12 7.11 Modification
Valves Standards Committee.”
7.13 7.12 Editorial Renumbered paragraph.
1 Scope
1.1 This Standard covers limitations on the selection of all valves normally classified
under Saudi Aramco Materials System (SAMS) Class 04. This will normally
include ball, butterfly, check, choke, diaphragm, gate, globe, needle, and plug
valves used for on-off, for manual control service or for prevention of reverse
flow, as appropriate.
1.2 Specifically excluded from the scope are:
a) Control, safety-relief, relief, surge relief, solenoid, pilot, and other valves
classified under SAMS Class 34.
b) Applications involving flues and chimneys, air conditioning and ventilation
ducts.
c) Drilling and wellhead valves classified under SAMS Class 45.
1.3 Where applicable, this Standard supplements the requirements of ASME B31,
Code for Pressure Piping.
2 Conflicts and Deviations
Any conflicts between this document and other applicable Mandatory Saudi Aramco
Engineering Requirements (MSAERs) shall be addressed to the EK&RD Manager.
Any deviation from the requirements herein shall follow internal company procedure
SAEP-302.
3 References
All referenced specifications, standards, codes, drawings, and similar material are
considered part of this engineering standard to the extent specified, applying the
latest version, unless otherwise stated.
3.1 Saudi Aramco References
Saudi Aramco Engineering Procedures
SAEP-29 General Instructions and Guidelines for Online Valve
Preventive Maintenance
SAEP-35 Valves Handling, Hauling, Receipt Tests, and Storage
SAEP-302 Waiver of a Mandatory Saudi Aramco Engineering
Requirement
Saudi Aramco Engineering Standards
SAES-A-007 Hydrostatic Testing Fluids and Lay-up Requirements
SAES-A-133 Internal Corrosion Protection Requirements
4.1 Valves and chokes shall be purchased in accordance with the Saudi Aramco
Regulated Vendors List (RVL).
4.2 The selection of valves and chokes shall normally be limited to the materials,
types and sizes that are listed in Saudi Aramco Materials System (SAMS) Class
04 specifications unless no suitable valve is listed.
4.3 Whenever applicable, the relevant Saudi Aramco Materials System
Specifications (SAMSS's) listed in Section 3 of this standard shall be included in
all requisitions.
4.4 At times it is necessary to purchase a valve that is generally similar to that
covered by an SAMSS but differing from it in some specific design, construction,
materials, or performance characteristics. In such cases, the SAMSS shall be
included in the purchase requisition in addition to the required modifications
provided that these modifications are in accordance with all other Mandatory
Saudi Aramco Engineering Requirements.
4.5 All requisitions, except those for API 6A valves and chokes, shall reference 04-
SAMSS-035 and 04-SAMSS-048. All requisitions for API 6A valves and chokes
shall reference 04-SAMSS-055.
4.6 Form SA-6233-1, Valve Data Sheet, shall be filled out for each non-SMG
(System Materials Group) line item and attached to every purchase requisition.
Note: For project reviews, list all Valve Data Sheets for 04-SAMSS valves and
chokes under Index L.
4.7 Field Tests
4.7.1 If requested by the Proponent (Operating organization), new valves designated
for isolation service (as specified by the Proponent Operating organization) shall
be subjected to a high pressure hydrostatic seat test prior to installation in the
line.
Note: The requirements in SAEP-35 are independent of the requirement above.
SAEP-35 mandates pressure testing of all valves which have been in long term
storage prior to installation.
4.7.2 Valves selected for seat testing shall be subjected to a shell pressure test at the
valve rated pressure unless otherwise agreed with the Proponent (Operating
organization).
4.7.3 Testing location shall be subject to Proponent (Operating organization)
acceptance. The test location shall be approved by Saudi Aramco Inspection
Department through a formal assessment.
4.7.4 A low pressure pneumatic seat test at 35 kPa (5 psig) shall be substituted for the
high pressure hydrostatic seat test for flare system valves.
4.7.5 Buttweld and socketweld end valves in nominal pipe size (NPS) 2-inches and
smaller are exempt from the above field testing requirements.
4.7.6 Test procedures, pressures, durations, and leakage acceptance criteria shall be
equal to those that the valves were originally purchased to, except for the shell
test pressure which should be limited to the valve rated pressure. All resilient
(soft) seated isolation valves shall have zero leakage.
4.7.7 If valves are subjected to field hydrotesting, see SAEP-35 and SAES-A-007. For
major projects where numerous valves are to be subjected to field hydrotesting,
a preservation package shall be developed and approved prior to the initiation of
any testing.
Note: Consider the valve features and materials at design stage and when
developing a preservation package, see SAES-A-133.
4.8 The use of ANSI/FCI 70.2 to specify seat leakage criteria for valves covered
under this engineering standard is not permitted.
Note: Chokes are exempt from this requirement.
4.9 Trim material includes the stem, the body and closure seating surfaces,
bushings, pins, springs, guides, and any other small parts in contact with the
service fluid.
4.10 Drain valves, valves at low points and body cavity auxiliary drains (piping and
valves) where water may collect under stagnant flow conditions shall be
addressed per the dead leg sections in SAES-L-310.
4.11 Handling, hauling, receiving inspection, and storage of valves and chokes shall
be in accordance with SAEP-35.
4.12 Preventive maintenance of valves and chokes shall be in accordance with
SAEP-29.
Note: Include critical valves in the SAEP-20, Equipment Inspection Schedule (EIS).
4.13 When a service type is referenced in this specification and no definition has been
provided, refer to the definition in API RP 615.
5 General Design Limitations
5.1 Bonnet/Cover
5.1.1 Pressure seal bonnet/cover designs are permitted in steam or other clean non-
corrosive services. The use of pressure seal bonnet/cover designs in other
services is only permitted if the body has been inlayed in the bonnet sealing area
with an 18-8 material or higher alloy suitable for the service.
5.1.2 Bonnets retained by split rings and sealed by means of an O-ring or a seal-
welded membrane are not permitted.
5.1.3 The use of welded bonnet valves in hydrocarbon services shall be limited to
NPS 4 and smaller provided it is approved by the Director of the responsible
operating department.
5.1.4 Screwed bonnet and screwed body valves shall not be used in any hydrocarbon
or hazardous material services unless the bonnets and body end connections
are tack welded to the body or provided with locking pin.
Exception: Choke bonnet designs that are self-locking by design (such as the Stub
ACME threaded type) can be exempted from the above requirement
provided the choke manufacturer has design calculations that
demonstrate the design is self-locking and the calculations have been
reviewed by an independent third-party certification body.
5.1.5 Straight-thru union body check valves shall be used only in portions of piping
systems where pipe unions are permissible.
5.1.6 Union bonnet valves shall not be used in any hydrocarbon or hazardous material
services.
5.2 End Connections
5.2.1 The requirements of SAES-L-110 are applicable to all valves.
5.2.2 Integral flanged valve bodies with tapped bolt holes shall not be used except with
specific approval of the Proponent (Operating organization). This requirement
does not apply to lug type valves.
Note: Integral flanged valve bodies with tapped bolt holes can be considered when
other options are not feasible or where there is a strong technical justification
for their use. Prior to using such designs, consider installation, removal and
potential for stuck bolting.
5.2.3 If requested by the Proponent (Operating organization), critical valves, welding
end valves, and others that cannot be removed from the line without serious
difficulty (e.g., in restrained pipelines), NPS 8 and larger, shall be of a type that
is repairable in the line such as a top-entry design.
5.2.4 When replacing existing valves with non-standard flange dimensions (such as
NPS 30 and larger in Class 1500), the Purchaser shall include the applicable
standard drawing in the purchase documents.
5.2.5 When raised face flanges are to be used for hydrogen service, the Purchaser
must specify the special flange face surface finish requirements per SAES-L-109
in the valve purchase documents.
5.3 Ratings
5.3.1 Valves utilizing soft seats do not necessarily follow ASME B16.5 or other industry
standard pressure-temperature (P-T) relationships at temperatures above 38°C.
The specific valve manufacturer’s literature shall be consulted when the
pressure-temperature ratings for higher temperatures have not been specified
by the relevant SAMSS or the Purchase Order.
5.3.2 In hydrocarbon services, the minimum body rating of threaded and socketweld
end NPS 2 and smaller valves shall be equivalent to API STD 602 Class 800.
5.4 Sizes
Valves shall be subject to the same size limitations specified for pipe in
SAES-L-136.
5.5 Stem Packing
Isolation valves NPS 3 and larger in hydrocarbon services shall not be provided with
pure polymer/elastomer stem packing or stem seals unless the valves have been
qualified as fire-safe.
5.6 Operator
5.6.1 The need for power actuation of all valves NPS 12 and larger in all pressure
classes shall be reviewed with the responsible operating organization.
5.6.2 Chainwheel operation shall not be provided for emergency isolation valves or
valves having a threaded body connection.
5.7 Installation
5.7.1 Gate valves with back-seats
Gate valves with back-seats shall not be installed with their stems below the
horizontal except in the following cases: (a) clean services, (b) when they function
as isolation valves in pressure relief and flare system piping, and (c) when in utility
or other similar non-critical services (firewater is considered to be critical service).
Critical / non-critical valves shall be specified by proponent (Operating organization).
5.7.2 Unidirectional Isolation valves
The blockage direction required during operation and also during maintenance shall
be considered prior to selecting unidirectional isolation valves.
Notes: Isolation valves that include an equalizing hole in the closure member to
connect the valve body cavity with the high-pressure (HP) side of the valve
when the closure member is in the closed position to relieve excess cavity
pressure are unidirectional designs. Such isolation valves are designed to
block flow when the pressure source is on the side of the valve designated HP.
It may not always be obvious to the valve installer(s) whether the marking on
a valve body (e.g., a directional arrow) indicates the direction of normal flow or
the direction of pressure against which the valve shall seal when in the closed
position. This can be opposite of the normal flow direction.
Care needs to be taken when interpreting directional arrows and marking on
valve bodies to ensure the valve is installed in the correct direction.
The system drawings (for example, piping isometrics or P&ID) shall show the valve
installation orientation with reference to the marking on the valve.
5.7.3 When ductile and cast-iron bodied valves are supplied with coating on the flange
gasket seating face, the gaskets used during valve installation shall be
compatible with the valve and pipe flange facing.
5.7.4 Seal welding
5.7.4.1 All threaded connections on valve bodies and associated piping shall be
seal welded.
Exceptions: Exceptions are those connections that are frequently
disassembled (such as vent and drain plugs) and those that are
adjacent to elements that contain small moving parts (such as
injection fittings and body relief valves).
5.7.4.2 Seal welding shall follow the general requirements of SAES-L-110.
6 Specific Valve Type Limitations
6.1 Ball and Plug Valves
Lever operated valves shall be equipped with a self-locking handle to prevent
accidental operation.
6.2 Butterfly Valves
6.2.1 Concentric butterfly valves, such as the API STD 609 Category A type (typically
with internal rubber linings), are permitted only in non-hydrocarbon applications.
6.2.2 The use of butterfly valves in hydrocarbon service shall be limited to a maximum
rating of Class 600 and clean service. Minimum requirements in hydrocarbon
service are as follows:
a) Valves shall be designed in accordance with API STD 609 Category B
with double or triple offset-type construction.
b) Valves shall be qualified fire-safe to either API SPEC 6FA, API STD 607,
or ISO 10497, except in applications where other components of the
system are not designed to be firesafe such as Single-Point-Mooring
(SPM) systems.
c) The body shall be of the lug-type design with tapped bolt holes or the
double-flanged type. Use of the wafer-type body is not permitted.
d) Valves shall be full-rated.
Exception: In systems where the normal operating pressure is 103 kPa
(15 psig) or less, the valve may be specified with half-rated trim
(approximately 50% of the full-rated pressure).
e) Valves shall be bi-directional, although they may have a “preferred”
direction. Valves shall be installed in the “preferred” direction indicated on
the valve.
6.3 Check Valves
6.3.1 Dual- and single-plate check and swing check valves shall not be used in
reciprocating pump and compressor suction and discharge services or similar
pulsating services.
6.3.2 A non-slam internal-spring-assisted nozzle type check valve shall be installed at
the discharge of pumps and compressors. Other check valve types shall be
supported by a hydraulic analysis to verify that the selected check valves have
the correct dynamic response to prevent slamming and limit pressure surge to
an acceptable level (the analysis shall include consideration of the “worst case”
operating mode scenario) and specifically approved by the Proponent (Operating
organization).
6.3.3 The service, design and operating scenarios, including minimum flowrate,
maximum flowrate and frequency, shall be included in the valve purchase
documents.
6.3.4 Check valve sizing and dynamic response characteristics shall be evaluated by
the system designer and the valve manufacturer to verify the suitability of the
selected check valves for the application.
6.3.5 If requested by the Proponent (Operating organization), for parallel pump
systems with individual pump discharge piping of NPS 20 and greater, a
hydraulic analysis shall be conducted to verify that the selected check valves
have the correct dynamic response to prevent slamming and limit pressure surge
to an acceptable level. The analysis shall include consideration of the “worst
case” operating mode scenario.
6.3.6 For piping NPS 4 and larger, a turbulence-free minimum distance of 5 pipe
diameters upstream and 2 pipe diameters downstream of every check valve shall
be maintained to minimize potential wear/damage to internal valve parts. Pipe
fittings (e.g., elbows, reducers, tees, etc.) or flow-restricting devices (e.g.,
orifices, control valves, etc.) shall not be installed in these zones unless the
shall meet the same requirement if they do not have graphite seals or their
standard specified leakage rate exceeds that of API STD 598.
7.6 Firewater Systems
Valves in firewater systems shall meet the requirements of SAES-B-017.
7.7 Drains and Vents
Atmospheric drain and vent valves shall be provided with a plug or blind on the
discharge side.
7.8 Storage Tanks and Vessels
Flangeless valves shall not be used as the first block valve against storage tanks
or vessels containing hydrocarbons or hazardous materials.
7.9 Scraper Trap Valves
7.9.1 Scraper trap mainline isolation valves shall be full bore through conduit gate or
ball valves in accordance with API SPEC 6D. The seating configuration shall
provide DIB-2 functionality unless otherwise approved by the Proponent
(Operating organization) on a case-by-case basis.
7.9.2 Drain valves shall be inverted pressure balanced lubricated plug valves with
hardfacing on the plug and body seating surfaces.
7.9.3 Kicker valves and vent valves shall be inverted pressure balanced lubricated plug
valves.
Exception: For API SPEC 6A services rated above 5,000 psi, metal seated ball
valves for isolation and chokes for throttling service may be used for
drain, kicker and vent valves, as appropriate.
7.9.4 Scraper trap isolation valves and kicker valves shall have:
(a) a minimum trim metallurgy of 22Cr Duplex Stainless Steel (UNS S31803);
and,
(b) the valve seat pockets for spring loaded seat designs only shall be
specified to have an Alloy 625 weld overlay.
The requirements of this paragraph override the materials requirements listed in
the Material Appendix, unless those are more stringent.
Note: An obturator (e.g., ball) in low alloy or carbon steel with corrosion resistant alloy
material weld overlaid on all process wetted surfaces is acceptable for meeting
the above requirement on valves larger than NPS 4.
7.10 Instrumentation Root Isolation Valves
7.10.1 Instrumentation root isolation valves shall be API STD 602 gate valves.
Exception: Modular piping class valve assemblies in 7.11.2 are an exception.
7.10.2 Modular valve assemblies consisting of a root isolation valve together with
bleed/vent and other types of valves (such as ball or needle) are permitted.
Prior to selecting a modular valve assembly, evaluate the likelihood and impact
of taking a modular valve assembly out of service when there is no separate root
valve.
Modular piping class valve assemblies incorporating needle or globe type valve
units disposed around the circumference of a body shall be restricted to
applications where scaling, waxing, or other fouling of the flow passages is
unlikely to occur, owing to the extremely convoluted flow passage.
Modular valve assemblies shall be of a piping class design of bolted bonnet
configuration.
Notes: Instrumentation class valve assemblies do not meet the requirements. Valve
designs with threaded spindle nut arrangements (e.g., EEMUA 182, 2nd
Edition, Figure 5.4.15) do not meet the requirements.
7.11 Steam Service
Isolation valves, NPS 2 and larger, in Class 600 and higher rated systems shall
be parallel slide gate valves equipped with a cavity pressure relief system.
7.12 Blowdown Valves
Blowdown valves in gas pipelines shall be plug valves.
7.13 Bypass/Equalization Valves
Mainline bypass/equalization valves in gas service shall be inverted pressure
balanced lubricated plug valves.
7.14 Buried Valves
Valves shall be an API SPEC 6D valve type which is designed for buried service
in accordance with the requirements in API SPEC 6D and 04-SAMSS-035.
Exceptions: Other valve types are permitted for buried service when specified and
designed with appropriate features (e.g., stem/shaft extension to raise
the operator above ground; extension casing/housing for protecting
extended stems/shafts; sealed interfaces to prevent ingress of external
contaminants and moisture; means of preventing pressure buildup in
stem extension casing/housing assemblies and operators resulting from
stem or bonnet seal leakage; position indicators; valve and auxiliaries
protected from external corrosion with suitable coating system in
accordance with SAES-H standards in Section 3).
Note: See SAES-L-110 for restrictions on flanged joints and SAES-L-109 for
requirements for protection of bolting.
7.15 Auto-Ignition services
Isolation valves shall be quarter turn non-rising stem designs.
Document History
16 February 2022 Major periodic revision.
19 February 2019 Major revision as it is due for regular update
1 March 2016 Revised the Next Planned
Materials Appendix
Table I - Service and Application Requirements Valve Body and Trim Materials
Conditions Valve Materials
Environment Conc.(%) Temp.(C) Body Trim Remarks
Carbon Dioxide
dry 100 0 - 150 CS 410
wet LT 100 5 - 90 316 316
Chlorine,
dry (12) 100 0 - 70 CS M400
M400 M400
wet (13) LT 100 0 - 70 CPVC CPVC
C-276 C-276 For castings, Alloy C-4
LT 10 0-49 PVC PVC is preferred to C-276
Table I (Cont'd)
Hydrocarbon Gas N/A -18 to 220 CS ENP ENP trim not permitted
including Khuff - 18 to 280 CS 410 for wet or sour gas
Gas (15, 18)
CS TC
Light Hydrocarbons 100 -18 to 220 CS ENP ENP trim not permitted for
(Butane, Ethane, -18 to 400 CS 410 wet or sour gas
Hexane, Methane, CS 316
Pentane and CS TC
Propane) and -45 to -18 LTS 316
NGL LT -45 304 304
316 316
Table I (Cont'd)
Conditions Valve Materials
Environment Conc.(%) Temp.(C) Body Trim Remarks
Sodium 50 5 - 50 D2 20
Hydroxide 316(X) 316(X)
50 - 80 CS M400
M400(X) M400 (2)
20 5 - 50 CS M400
304L(X) 304L(X)
7 5 - 80 CS 316
CS M400
7 80 - 100 M400 M400
Water
Non-corrosive N/A 0 - 100 CS 410 Includes deaerated and/or
(oxygen free or D1 (7) Br inhibited sea, raw, well water
(inhibited) Br Br Zeolite softened, chilled, and
CS 316 boiler feed water. pH GT 6,
oxygen LT 25 ppb
Table I (Cont'd)
Conditions Valve Materials
Environment Conc.(%) Temp.(C) Body Trim Remarks
General Notes:
(A) All valve designs shall incorporate features required to resist galling of mating surfaces by means of necessary
hardness differentials, weld overlays, galling resistant material combinations, etc.
(B) Trim material includes the stem, the body and closure seating surfaces, bushings, pins, springs, guides, or any
small parts in contact with the service fluid.
(C) The gate, disc, piston, ball, or plug that provide closure are normally made from the “trim” material in smaller valve
sizes (less than about 6 inches). The closure may be made from material equivalent to the valve body except
that the closure seating surfaces shall be of the material having a corrosion resistance equal to or “better” than
the trim.
(D) See Table IV(a), (b) and (c) for material designations.
(E) LT means “Less Than”, GT means “Greater Than.”
(F) (X) indicates materials for critical applications such as hazardous service, poor accessibility for maintenance, or
significant loss of production in the event of failure.
(G) Austenitic (“300 Series”) stainless steel components that are to be welded or weld overlaid shall be low carbon
(.03% carbon maximum) grades. Low carbon grades may be substituted for regular carbon grades, but not vice
versa.
(H) In making the material selections, consider all internal and external environmental factors, production/process
variables, changes during the design life, and the additional limitations and requirements in SAES-L-132,
SAES-A-133 and SAES-A-134.
(I) All materials for valves and chokes in sour service shall meet the requirements of NACE MR0175/ISO 15156.
Only use NACE MR0103 to define sour service in refinery process environments; see SAES-A-133 and
SAES-L-132.
Table I (Cont'd)
Specific Notes:
(2) Alloy K-500 may be substituted for Alloy 400 where additional hardness or strength is required.
(6) Do not expose stainless-steel trim to HCl acid-cleaning.
(7) Gray cast iron valve bodies may be substituted for ductile iron. However, ductile iron is preferred.
(8) Sulfuric acid concentrations over 100% (“Oleum”) contain free sulfur trioxide.
(10) Inhibited against stress corrosion cracking of steel with minimum 2,000 ppm water.
(12) Dry chlorine contains less than 2,000 ppm water; do not use with titanium components.
(13) Wet chlorine contains at least 2,000 ppm water.
(14) These services are subject to additional considerations such as galvanic compatibility, velocity effects or
additional water chemistry factors. For example, high velocities or low pH may dictate against the use of bronze
trim or Ductile Iron (DI) bodies. Copper alloy bodied valves shall not be used with carbon steel pipe in corrosive
water service without the use of insulating sets.
(15) Materials for valves in wet sour service shall meet the requirements of NACE MR0175/ISO 15156.
NACE MR0175/ISO 15156 defines sour service. See also SAES-A-133.
(16) See Nelson Charts for details concerning the influence of temperature and partial pressure of hydrogen on
material selection.
(18) Body materials for Khuff Gas valves are per API 6A. Drain valves and valves at low points where water may
collect under stagnant conditions shall be addressed per the dead leg sections in SAES-L-310.
(20) Where indicated, the zinc content of wetted copper alloy components shall be 16% or less.
(21) Availability of bronze valves in ratings above Class 150 is limited, and have not yet been tried in Saudi Aramco.
(22) Linings are generally used in butterfly valves, non-lubricated plug valves, and some wedge gate valves. Coatings
are used on ball, check, globe and gate valves; internal coatings shall be in accordance with SAES-H-002 and
04-SAMSS-035.
(23) Sour brine services may require specification of NACE MR0175/ISO 15156.
(24) Use ductile iron body, if available, for butterfly valves in non-hydrocarbon services.
(26) For potable water service, carbon steel body valves with SS316 trim are allowed in NPS 4-inch and above only.
For critical service, use coated or lined valves.
(27) Type 316 trim is only acceptable when there is a high degree of confidence that occasional oxygen ingress cannot
occur due to startup conditions, pump or valve packing leaks, etc. All trim shall be full SS316.
(28) Carbon steel overlaid with Alloy 625 may be substituted for super austenitic or duplex stainless steels (SSS)
provided that (a) the entire exposed area is overlaid and (b) the fused material has no more than 30% dilution.
(29) Where seawater is chlorinated, residual chlorine should be limited to 2 ppm or less for SSS alloys rated A in
Table IV-B, 1 ppm for those rated B, and 0.5 ppm for those rated C. Where residual chlorine exceeds 2 ppm,
the Alloy C family of alloys in Table IV-A should be considered.
(30) For refinery applications, follow SAES-L-132, Table 2.
(31) Materials for drinking water applications shall be in accordance with National Sanitation Foundation (NSF 61).
The stem and spring alloys listed below may be used in valves having the trim materials
specified in Table I. These alloys usually may be fabricated to the required strength levels
more readily than the general trim materials and their corrosion resistance is
approximately equal to or better than that of the corresponding general trim.
Alternate Alternate
Specified Trim Stem Materials Spring Materials (2)
Stainless Steels
410 17-4, A286 17-4, X750, 600
6NM 17-4, A286 17-4, X750, 600
304 17-4, A286 17-4, X750, 600
316 N50, 718 718, R30035, Elg
20 625 R30035, Elg, 625, C-276
SSS 625 R30035, Elg, 625, C-276
Notes:
(1) A specialized application for gaseous chlorine service.
(2) Iron base alloy springs shall not be used in sour service.
Acid, Nitric
to 100% PTFE/Elastomer (3) FFKM CPE, PTFE, FEP
to 60% Fluorocarbon Elastomer CPVC, CPE
Acid, Phosphoric EPDM, IIR, CR, NR, CSM PVC, CPVC, PE, PP,
CPE, PVDC
Acid, Sulfuric
90%+ CSM PVDC, CPE
LT 60% CR, CSM, IIR, EPDM PVDC, CPE, CPVC
Ammonia (8) Any except amine cured FKM, TFE/P Any except Nylon
Amines (MEA, DEA, DGA, VMQ, EPDM, T, OT, EOT, CSM FEP, PTFE
ADIP) (8) (amine cured FKM, TFE/P not suitable)
Crude Oil
to 50°C Fluorocarbon Elastomers PVC, CPVC, PP, PPS
to 200°C Fluorocarbon Elastomers Fluorocarbon Plastics
Gasoline, MTBE blend NBR (min. 40% acrylonitrile), HNBR, FFKM Fluorocarbon plastics
Hydrogen Sulfide T, OT, EOT, CSM, EPDM PE, PP, PVC, PVDF
Hypochlorite, Ca/Na Butyl, CSM, CR, CO, ECO, GECO, EPDM PVC, CPVC, PVDC
Light Hydrocarbons T, OT, EOT, CO, ECO, GECO, FKM, Fluorocarbon Plastics, PPS
(Butane, Ethane, Methane, FMQ, FVMQ
Pentane, Propane)
Sewage, Oily CR, NBR, HNBR, , T, OT, EOT PVC, CPVC, PVDC
Sodium Hydroxide Any except FKM and TFE/P Any except PVDC
at high conc.
Notes:
(1) Temperatures are 49°C or less unless otherwise indicated.
(2) See Table IV-A, B and C for material designations.
(3) “Elastomer” indicates any backup elastomer within the permissible temperature range.
20 Alloy 20 N08020
CS Carbon Steel -
DI Ductile Iron -
TC Tungsten Carbide -
Ti Titanium (Unalloyed) -
Notes:
(1) Copper alloys shall have 16% or less zinc when used in corrosive aqueous service.
(2) Reference: 04-SAMSS-003.
(3) CA6NM Stainless Steel may be substituted for Type CA15 (AISI 410) for cast valve components.
Alloy Generic/Popular
Designation Name Form UNS No. Spec or Grade
SSS Superaustenitic
BR Copper Alloys
Notes:
(1) SSS alloy rankings for pitting and crevice corrosion resistance are shown in parentheses next to the name, (A)
being best. SSS alloys for seawater or sour brine service must be those ranked (A).
(2) ASTM B148 components for seawater service shall receive a temper anneal heat treatment per ASTM B601
Condition “TB”.
Material
Designation Generic Names Chemical Name
PLASTICS
PE Polyethylene Polyethylene
PP Polypropylene Polypropylene
PVDF Polyvinylidenefluoride
ECTFE Ethylene-Chlorotrifluoro-Ethylene
CTFE Chlorotrifluoro-Ethylene
PTFE Polytetrafluoro-Ethylene
Nylon Polyamide
PEEK Polyetheretherketone
ELASTOMERS
CR Chloroprene Poly-Chloroprene
EPDM Ethylene-Propylene
Material
Designation Generic Names Polymer
ELASTOMERS (Cont'd)
FLUOROCARBON-ELASTOMERS
FFKM Perfluoroelastomer
TFE/P Tetrafluoroethylene-Propylene
Note:
* FMQ and FVMQ are NOT categorized as fluorocarbon elastomer.