ASTM F3386/F3386M-21
(Specification)Standard Specification for Detonation Flame Arresters
Standard Specification for Detonation Flame Arresters
SCOPE
1.1 This specification provides the minimum requirements for design, construction, performance, and testing of detonation flame arresters intended to protect against deflagrations, overdriven (unstable) detonations, stable detonations, and stabilized burning.
1.2 This specification is intended for detonation flame arresters installed in vapor control systems at Marine Facilities subject to the requirements in 33 CFR, Part 154, Subpart P — Marine Vapor Control Systems.
Note 1: In 1990, by permission from ASTM International, an earlier draft of this specification was incorporated and printed in 33 CFR, Part 154, Appendix A.
1.3 This specification is intended for detonation flame arresters protecting systems containing gases or vapors of liquids with flash points 140°F [60°C] (closed cup) or less. The tests in this specification are intended to qualify detonation flame arresters for all in-line applications, provided the operating pressure is equal to or less than the maximum operating pressure stated in the manufacturer’s certification, and the diameter of the piping system in which the detonation flame arrester is to be installed is equal to or less than the piping diameter used in the testing.
1.4 This specification is limited to detonation flame arresters operating at temperatures no greater than 140°F [60°C], unless the detonation flame arresters are tested at the higher operating temperatures.
Note 2: Refer to UL 525 for additional requirements that may be applicable.
1.5 The values stated in either SI units or inch-pound units are to be regarded separately as standard. The values stated in each system are not necessarily exact equivalents; therefore, to ensure conformance with the standard, each system shall be used independently of the other, and values from the two systems shall not be combined.
1.6 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety, health, and environmental practices and determine the applicability of regulatory limitations prior to use.
1.7 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
General Information
- Status
- Published
- Publication Date
- 30-Apr-2021
- Technical Committee
- F25 - Ships and Marine Technology
- Drafting Committee
- F25.11 - Machinery and Piping Systems
Relations
- Refers
ASTM F1155-10(2019) - Standard Practice for Selection and Application of Piping System Materials - Effective Date
- 01-Dec-2019
- Refers
ASTM F1155-10(2015) - Standard Practice for Selection and Application of Piping System Materials - Effective Date
- 01-May-2015
- Effective Date
- 01-Nov-2014
- Effective Date
- 01-Apr-2014
- Effective Date
- 15-Dec-2010
- Effective Date
- 01-May-2009
- Effective Date
- 01-Nov-2008
- Effective Date
- 01-Nov-2004
- Refers
ASTM F1155-98(2004) - Standard Practice for Selection and Application of Piping System Materials - Effective Date
- 01-Nov-2004
- Effective Date
- 01-Oct-2004
- Effective Date
- 10-Dec-1999
- Effective Date
- 10-Dec-1999
- Effective Date
- 10-Apr-1998
- Effective Date
- 01-Jan-1993
Overview
ASTM F3386/F3386M-21: Standard Specification for Detonation Flame Arresters establishes the minimum criteria for the design, construction, performance, and testing of detonation flame arresters. These safety devices play a crucial role in preventing the propagation of flames and detonations in vapor control systems, especially at marine facilities covered under 33 CFR, Part 154, Subpart P-Marine Vapor Control Systems. The standard addresses both deflagrations and detonations, including unstable or overdriven detonations and stabilized burning, in systems containing gases or vapors from liquids with flash points of 140°F (60°C) or less.
This specification is applicable to detonation flame arresters operating at temperatures up to 140°F (60°C), unless tested and certified for higher temperatures. The requirements harmonize safety considerations, performance expectations, and regulatory compliance for equipment used in hazardous environments.
Key Topics
Design and Construction: The standard outlines strict material criteria for pressure-retaining components, including requirements for resistance to corrosion, temperature, and system pressures. Only certain metallic materials are allowed for pressure parts, with additional provisions to prevent galvanic corrosion and ensure safe joint construction.
Performance and Testing: Extensive prototype testing is mandated, assessing resistance to corrosion, hydrostatic pressure, pneumatic pressure, and the module’s ability to arrest both deflagrations and detonations. Both Type I (capable of withstanding stationary flames) and Type II (for applications where stationary flames are unlikely, with additional safety methods) flame arresters are covered.
Installation and Operation: Manufacturer’s documentation must include installation, operation, and maintenance instructions, as well as descriptions of all configurations tested. Marking requirements ensure traceability and proper device identification in the field.
Certification and Quality Assurance: Products must be certified to meet the standard, with supporting test reports and clear markings for operational limits, manufacturer details, and model identification. Ongoing quality assurance processes ensure consistency between tested prototypes and production units.
Applications
Detonation flame arresters specified under ASTM F3386/F3386M-21 are critical safety devices in:
- Marine Vapor Control Systems: Required at marine loading terminals and similar facilities to prevent flame transmission in vapor recovery and processing systems handling flammable or combustible liquids.
- Cargo Tank and Bulk Storage Operations: Used where volatile liquids with low flash points are stored, transferred, or processed.
- Petroleum and Chemical Facilities: Protect pipelines, storage tanks, and process lines carrying explosive or flammable gases and vapors.
- Hazardous Material Transfer Operations: Ensure safe transfer and vapor management for compliant operations under federal regulations.
Compliance with this standard helps satisfy relevant regulatory requirements, including those set by the US Coast Guard and referenced in federal regulations. These arresters are often required for obtaining operational permits and for ongoing safety management.
Related Standards
For comprehensive compliance and compatibility checks, consider the following related standards and regulatory documents:
- UL 525: Standard for Flame Arresters – For additional requirements relevant to flame arresters.
- ASME B16.5: Pipe Flanges and Flanged Fittings
- ASME Boiler and Pressure Vessel Code, Sections VIII and IX – For material and fabrication requirements.
- ASTM A395/A395M: Ferritic Ductile Iron Pressure-Retaining Castings
- ASTM F722: Welded Joints for Shipboard Piping Systems
- ASTM F1155: Selection and Application of Piping System Materials
- IEC 60079-20-1: Material Characteristics for Gas and Vapour Classification
- 33 CFR, Part 154: Regulations for Facilities Transferring Oil or Hazardous Material in Bulk
The ASTM F3386/F3386M-21 standard is integral for industries that need to ensure flame and detonation protection in vapor systems, contributing significantly to operational safety and regulatory compliance.
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Frequently Asked Questions
ASTM F3386/F3386M-21 is a technical specification published by ASTM International. Its full title is "Standard Specification for Detonation Flame Arresters". This standard covers: SCOPE 1.1 This specification provides the minimum requirements for design, construction, performance, and testing of detonation flame arresters intended to protect against deflagrations, overdriven (unstable) detonations, stable detonations, and stabilized burning. 1.2 This specification is intended for detonation flame arresters installed in vapor control systems at Marine Facilities subject to the requirements in 33 CFR, Part 154, Subpart P — Marine Vapor Control Systems. Note 1: In 1990, by permission from ASTM International, an earlier draft of this specification was incorporated and printed in 33 CFR, Part 154, Appendix A. 1.3 This specification is intended for detonation flame arresters protecting systems containing gases or vapors of liquids with flash points 140°F [60°C] (closed cup) or less. The tests in this specification are intended to qualify detonation flame arresters for all in-line applications, provided the operating pressure is equal to or less than the maximum operating pressure stated in the manufacturer’s certification, and the diameter of the piping system in which the detonation flame arrester is to be installed is equal to or less than the piping diameter used in the testing. 1.4 This specification is limited to detonation flame arresters operating at temperatures no greater than 140°F [60°C], unless the detonation flame arresters are tested at the higher operating temperatures. Note 2: Refer to UL 525 for additional requirements that may be applicable. 1.5 The values stated in either SI units or inch-pound units are to be regarded separately as standard. The values stated in each system are not necessarily exact equivalents; therefore, to ensure conformance with the standard, each system shall be used independently of the other, and values from the two systems shall not be combined. 1.6 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety, health, and environmental practices and determine the applicability of regulatory limitations prior to use. 1.7 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
SCOPE 1.1 This specification provides the minimum requirements for design, construction, performance, and testing of detonation flame arresters intended to protect against deflagrations, overdriven (unstable) detonations, stable detonations, and stabilized burning. 1.2 This specification is intended for detonation flame arresters installed in vapor control systems at Marine Facilities subject to the requirements in 33 CFR, Part 154, Subpart P — Marine Vapor Control Systems. Note 1: In 1990, by permission from ASTM International, an earlier draft of this specification was incorporated and printed in 33 CFR, Part 154, Appendix A. 1.3 This specification is intended for detonation flame arresters protecting systems containing gases or vapors of liquids with flash points 140°F [60°C] (closed cup) or less. The tests in this specification are intended to qualify detonation flame arresters for all in-line applications, provided the operating pressure is equal to or less than the maximum operating pressure stated in the manufacturer’s certification, and the diameter of the piping system in which the detonation flame arrester is to be installed is equal to or less than the piping diameter used in the testing. 1.4 This specification is limited to detonation flame arresters operating at temperatures no greater than 140°F [60°C], unless the detonation flame arresters are tested at the higher operating temperatures. Note 2: Refer to UL 525 for additional requirements that may be applicable. 1.5 The values stated in either SI units or inch-pound units are to be regarded separately as standard. The values stated in each system are not necessarily exact equivalents; therefore, to ensure conformance with the standard, each system shall be used independently of the other, and values from the two systems shall not be combined. 1.6 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility of the user of this standard to establish appropriate safety, health, and environmental practices and determine the applicability of regulatory limitations prior to use. 1.7 This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
ASTM F3386/F3386M-21 is classified under the following ICS (International Classification for Standards) categories: 13.220.99 - Other standards related to protection against fire. The ICS classification helps identify the subject area and facilitates finding related standards.
ASTM F3386/F3386M-21 has the following relationships with other standards: It is inter standard links to ASTM F1155-10(2019), ASTM F1155-10(2015), ASTM F722-82(2014), ASTM A395/A395M-99(2014), ASTM F1155-10, ASTM A395/A395M-99(2009), ASTM F722-82(2008), ASTM F722-82(2004), ASTM F1155-98(2004), ASTM A395/A395M-99(2004), ASTM A395/A395M-99e1, ASTM A395/A395M-99, ASTM F1155-98, ASTM F722-82(1998). Understanding these relationships helps ensure you are using the most current and applicable version of the standard.
ASTM F3386/F3386M-21 is available in PDF format for immediate download after purchase. The document can be added to your cart and obtained through the secure checkout process. Digital delivery ensures instant access to the complete standard document.
Standards Content (Sample)
This international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principles for the
Development of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
Designation: F3386/F3386M −21 An American National Standard
Standard Specification for
Detonation Flame Arresters
ThisstandardisissuedunderthefixeddesignationF3386/F3386M;thenumberimmediatelyfollowingthedesignationindicatestheyear
of original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval.
A superscript epsilon (´) indicates an editorial change since the last revision or reapproval.
1. Scope* 1.6 This standard does not purport to address all of the
safety concerns, if any, associated with its use. It is the
1.1 This specification provides the minimum requirements
responsibility of the user of this standard to establish appro-
for design, construction, performance, and testing of detona-
priate safety, health, and environmental practices and deter-
tion flame arresters intended to protect against deflagrations,
mine the applicability of regulatory limitations prior to use.
overdriven (unstable) detonations, stable detonations, and sta-
1.7 This international standard was developed in accor-
bilized burning.
dance with internationally recognized principles on standard-
1.2 This specification is intended for detonation flame
ization established in the Decision on Principles for the
arresters installed in vapor control systems at Marine Facilities
Development of International Standards, Guides and Recom-
subject to the requirements in 33 CFR, Part 154, Subpart P —
mendations issued by the World Trade Organization Technical
Marine Vapor Control Systems.
Barriers to Trade (TBT) Committee.
NOTE 1—In 1990, by permission from ASTM International, an earlier
2. Referenced Documents
draft of this specification was incorporated and printed in 33 CFR, Part
154, Appendix A. 2
2.1 ASTM Standards:
1.3 This specification is intended for detonation flame A395/A395M Specification for Ferritic Ductile Iron
arresters protecting systems containing gases or vapors of
Pressure-Retaining Castings for Use at ElevatedTempera-
liquids with flash points 140°F [60°C] (closed cup) or less.The tures
tests in this specification are intended to qualify detonation
F722 Specification for Welded Joints for Shipboard Piping
flame arresters for all in-line applications, provided the oper- Systems
ating pressure is equal to or less than the maximum operating
F1155 Practice for Selection and Application of Piping
pressure stated in the manufacturer’s certification, and the System Materials
diameter of the piping system in which the detonation flame
2.2 ASME Standards:
arrester is to be installed is equal to or less than the piping
ASME B16.5 Pipe Flanges and Flanged Fittings: NPS 1/2
diameter used in the testing.
through NPS 24 Metric/Inch Standard
ASME Boiler and Pressure Vessel Code Section VIII,
1.4 Thisspecificationislimitedtodetonationflamearresters
Division 1
operating at temperatures no greater than 140°F [60°C], unless
ASME Boiler and Pressure Vessel Code Section IX
the detonation flame arresters are tested at the higher operating
temperatures.
2.3 Code of Federal Regulations (CFR):
Title 33, Part 154 Facilities Transferring Oil or Hazardous
NOTE 2—Refer to UL 525 for additional requirements that may be
Material in Bulk
applicable.
2.4 UL Standards:
1.5 The values stated in either SI units or inch-pound units
UL 525 Standard for Flame Arresters
are to be regarded separately as standard. The values stated in
each system are not necessarily exact equivalents; therefore, to
ensure conformance with the standard, each system shall be
For referenced ASTM standards, visit the ASTM website, www.astm.org, or
used independently of the other, and values from the two
contact ASTM Customer Service at service@astm.org. For Annual Book of ASTM
systems shall not be combined.
Standards volume information, refer to the standard’s Document Summary page on
the ASTM website.
Available from American Society of Mechanical Engineers (ASME), ASME
International Headquarters, Two Park Ave., New York, NY 10016-5990, http://
This specification is under the jurisdiction of ASTM Committee F25 on Ships www.asme.org.
and Marine Technology and is the direct responsibility of Subcommittee F25.11 on Available from U.S. Government Printing Office, Superintendent of
Machinery and Piping Systems. Documents, 732 N. Capitol St., NW, Washington, DC 20401-0001, http://
Current edition approved May 1, 2021. Published June 2021. Originally www.access.gpo.gov.
approved in 2019. Last previous edition approved in 2020 as F3386/F3386M – 20. Available from Underwriters Laboratories (UL), UL Headquarters, 333 Pfing-
DOI: 10.1520/F3386_F3386M-21. sten Road, Northbrook, IL, 60062, http://www.ul.com.
*A Summary of Changes section appears at the end of this standard
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
F3386/F3386M − 21
2.5 Other Documents: 4. Classification
International Electrotechnical Commission: 60079-20-1 Ex-
4.1 The two types of detonation flame arresters covered in
plosiveAtmospheres – Part 20-1: Material Characteristics
this specification are classified as follows:
for Gas and Vapour Classification – Test Methods and
4.1.1 Type I—Detonation flame arresters acceptable for
Data
applications where stationary flames may rest on the device.
4.1.2 Type II—Detonation flame arresters acceptable for
3. Terminology
applications where stationary flames are unlikely to rest on the
3.1 Definitions: device, and further methods are provided to prevent flame
3.1.1 ∆P/P,n—the dimensionless ratio, for any deflagra- passage when a stationary flame occurs. One example of
o
tion and detonation test in 9.3, of the maximum pressure “further methods” is a temperature monitor which activates a
increase (the maximum pressure minus the initial pressure), as fire safe automatic shutoff valve.
measured in the piping system on the side of the detonation
flame arrester where ignition begins by the device described in
5. Ordering Information
9.3.3, to the initial absolute pressure in, P , the piping system.
o
5.1 Orders for detonation flame arresters under this specifi-
cation shall include the following information as applicable:
3.1.1.1 Discussion—The initial pressure should be greater
5.1.1 Type (I or II),
than or equal to the maximum operating pressure specified in
5.1.2 Nominal pipe size,
11.1.6.
5.1.3 Each gas or vapor in the system and the corresponding
3.1.2 deflagration, n—a combustion wave that propagates
MESG,
subsonically (as measured at the pressure and temperature of
5.1.4 Inspection and tests in addition to those specified by
the flame front) by the transfer of heat and active chemical
this standard,
species to the unburned gas ahead of the flame front.
5.1.5 Anticipated ambient air temperature range,
3.1.3 detonation, n—areactioninacombustionwavepropa-
5.1.6 Purchaser’s inspection requirements (see 10.1),
gating at sonic or supersonic (as measured at the pressure and
5.1.7 Description of installation,
temperature of the flame front) velocity and characterized by a
5.1.8 Materials of construction (see Section 6),
shock wave.
5.1.9 Maximumflowrateandthemaximumdesignpressure
3.1.3.1 Discussion—A detonation is stable when it has no
drop for that maximum flow rate, and
significant variation of velocity and pressure or may be
5.1.10 Maximum operating pressure.
unstable during the transition of a combustion process from a
deflagration into a stable detonation. The transition occurs in a
6. Materials
limited spatial zone, where the velocity of the combustion
6.1 Thedetonationflamearresterhousing,andotherpartsor
wave is not constant and where the explosion pressure is
bolting used for pressure retention, shall be constructed of
significantly higher than in a stable detonation. When a
materials listed in Practice F1155, or Section VIII, Division 1,
deflagrationtransitionstoadetonation,itmustpassthroughthe
of the ASME Boiler and Pressure Vessel Code. Cast and
overdriven or unstable phase before becoming stable.
malleable iron shall not be used; however, ductile cast iron in
3.1.4 detonation flame arrester, n—a device which prevents
accordance with Specification A395/A395M may be used.
the transmission of a detonation and a deflagration.
6.2 Detonation flame arresters, elements, gaskets, and seals
3.1.5 flame passage, n—the transmission of a flame through
must be made of materials resistant to attack by seawater and
a device.
the liquids and vapors contained in the system being protected
3.1.6 flame speed, n—the speed at which a flame propagates
(see 5.1.3).
along a pipe or other system.
6.3 Nonmetallic materials, other than gaskets and seals,
3.1.7 gasoline vapors, n—a non-leaded petroleum distillate
shall not be used in the construction of pressure-retaining
consisting essentially of aliphatic hydrocarbon compounds
components of the detonation flame arrester.
with a boiling range approximating 149 to 167°F [65 to 75°C].
6.4 Nonmetallic gaskets and seals shall be non-combustible
3.1.8 marine facility, n—a facility as defined in 33 CFR,
and suitable for the service intended.
Part 154.
6.5 Bolting materials, other than those in 6.1, shall be at
3.1.9 maximum experimental safe gap (MESG), n—the
least equal to those listed in Table 1 of ASME B16.5.
maximum clearance between two parallel metal surfaces that
has been found, under specified test conditions, to prevent an
6.6 Thepossibilityofgalvaniccorrosionshallbeconsidered
explosion in a test chamber from being propagated to a
in the selection of materials.
secondary chamber containing the same gas or vapor at the
6.7 All other parts shall be constructed of materials suitable
same concentration.
for the service intended.
7. Other Requirements
Available from International Electrotechnical Commission (IEC), 3, rue de
7.1 Detonation flame arrester housings shall be gas-tight to
Varembé, 1st floor, P.O. Box 131, CH-1211, Geneva 20, Switzerland, https://
www.iec.ch. prevent the escape of vapors.
F3386/F3386M − 21
7.2 Detonation flame arrester elements shall fit in the facilities, personnel, and calibrated instruments that are neces-
housing in a manner that will ensure tightness of metal-to- sary to test detonation flame arresters in accordance with this
metal contacts in such a way that flame cannot pass between specification.
the element and the housing. 8.1.1 Atest report shall be prepared by the laboratory which
7.2.1 The net free area through detonation flame arrester shall include:
elements shall be at least 1.5 times the cross-sectional area of 8.1.1.1 Detailed drawings of the detonation flame arrester
the arrester inlet. and its components (including a parts list identifying the
materials of construction).
7.3 Housings, elements, and seal gasket materials shall be
8.1.1.2 Types of tests conducted and results obtained. This
capable of withstanding the maximum and minimum pressures
shall include the maximum temperature reached and the length
and temperatures to which the device may be exposed under
of testing time in 9.2 in the case of Type II detonation flame
both normal and the specified fire test conditions in Section 9
arresters.
and shall be capable of withstanding the corrosion test in 8.2.2,
8.1.1.3 Description of approved attachments (see 8.2.7).
the hydrostatic pressure test in 8.2.3, the pneumatic test in
8.1.1.4 Types of gases or vapors for which the detonation
8.2.10, and the production tests in 10.3.
flame arrester is approved.
7.4 Threaded or flanged pipe connections shall comply with
8.1.1.5 Drawings of the test rig.
the applicable ASME B16 standards in accordance with
8.1.1.6 Initial test pressure and test temperature.
Practice F1155. Welded joints shall comply with Specification
8.1.1.7 Record of all markings found on the tested detona-
F722.
tion flame arrester.
7.5 All flat joints of the housing shall be machined true and
8.1.1.8 A report number.
shall provide for a joint having adequate metal-to-metal
8.2 One of each model Type I and Type II detonation flame
contact.
arrester shall be tested. Where approval of more than one size
7.6 Where welded construction is used for pressure- of a detonation flame arrester design series is desired, only the
retaining components, welded joint design details, welding and
largest, smallest, and one intermediate size of the design series
non-destructive testing shall be in accordance with Section need be tested provided it is demonstrated by calculation or
VIII, Division 1, of the ASME Code and Specification F722.
other testing, or both, that the other intermediate size devices
Welders and weld procedures shall be qualified in accordance have equal or greater strength to withstand the force of a
with Section IX of the ASME Code.
detonation and have equivalent detonation arresting character-
istics.Achange of design, material, or construction which may
7.7 The design of detonation flame arresters shall allow for
affect the corrosion resistance or ability to resist endurance
ease of inspection and removal of internal elements if
burning, deflagrations or detonations shall be considered a
necessary, for such operation as cleaning, repair or replace-
change of model for the purpose of this paragraph.
ment.
8.2.1 The detonation flame arrester shall have the same
7.8 Detonation flame arresters shall allow for efficient
dimensions, configuration, and most unfavorable clearances
drainage of condensate without impairing their efficiency to
expected in production units. If a test device is modified during
prevent the passage of flame. The housing may be fitted with
the test program, the testing shall be started over again.
one or more drain plugs for this purpose. The design of a drain
8.2.2 A corrosion test shall be conducted. In this test, a
plug shall be such that by cursory visual inspection it is
complete detonation flame arrester, including a section of pipe
obvious whether the drain was left open.
similar to that to which it will be fitted, shall be exposed to a
20 % sodium chloride solution spray at a temperature of 77°F
7.9 All fastenings shall be protected against loosening.
[25°C] for a period of 240 h and allowed to dry for 48 h.
7.10 Detonation flame arresters shall be designed and con-
Following this exposure, all movable parts shall operate
structed to minimize the effect of fouling under normal
properly and there shall be no corrosion deposits which cannot
operating conditions.
be washed off.
7.11 Detonation flame arresters shall be capable of operat-
8.2.3 The detonation flame arrester shall be subjected to a
ing over the full range of ambient air temperatures anticipated.
hydrostatic pressure test of at least 350 psig [2.4 MPa] for 10
min without rupturing, leaking, or showing permanent distor-
7.12 Detonation flame arresters shall be of first class work-
tion.
manship and free from imperfections which may affect their
8.2.4 Flow characteristics as declared by the manufacturer
intended purpose.
shall be demonstrated by appropriate tests.
7.13 Detonation flame arresters shall be tested in accor-
8.2.5 Detonation flame arresters shall be subjected to tests
dance with the tests described in Section 8.
fordeflagration,detonation,andenduranceburn,inaccordance
with the test procedures in Section 9. The same detonation
8. Prototype Tests
flame arrester shall be used for all tests. Type I detonation
8.1 Tests shall be conducted by an independent laboratory flame arresters shall show no flame passage when subjected to
capable of performing the tests. The manufacturer, in choosing all three tests. Type II detonation flame arresters shall show no
a laboratory, accepts that it is a qualified independent labora- evidence of flame passage during the detonation/deflagration
tory by determining that it has (or has access to) the apparatus, tests in 9.3. Type II detonation flame arresters shall be tested
F3386/F3386M − 21
forenduranceburninaccordancewith9.2.Fromtheendurance detonation flame arrester shall be installed in the position for
burn test of a Type II detonation flame arrester, the maximum which it is designed and which will cause the most severe
temperature reached and the test duration shall be recorded and heating of the device under the prescribed endurance burn
provided as part of the laboratory test report. conditions. In this position the mixture shall be ignited.
8.2.6 When tested in accordance with Section 9, detonation
NOTE 3—The test apparatus shown in Fig. 1 shall be modified to allow
flame arresters shall prevent the transmission of flame and
the endurance burn test to be conducted at a test pressure higher than
detonation flame arrester housings shall be able to withstand,
atmospheric pressure, if required (see 5.1.4).
without damage or permanent deformation, the internal pres-
9.2.1.2 Endurance burn test shall start by using the appro-
sure and temperatures resulting from both stable and over-
priate most easily ignitable test media/air mixture (see 9.1)
driven (unstable) detonations and endurance burning.
with the aid of a continuously operated pilot flame or a
8.2.7 Where a detonation flame arrester is provided with
continuously operated igniter at the outlet. The flammable
cowls, weather hoods and deflectors, etc., it shall be tested in
mixture may be reignited as necessary in the course of the
each configuration in which it is provided.
endurance burn.The temperature of the test g
...
This document is not an ASTM standard and is intended only to provide the user of an ASTM standard an indication of what changes have been made to the previous version. Because
it may not be technically possible to adequately depict all changes accurately, ASTM recommends that users consult prior editions as appropriate. In all cases only the current version
of the standard as published by ASTM is to be considered the official document.
Designation: F3386/F3386M − 20 F3386/F3386M − 21 An American National Standard
Standard Specification for
Detonation Flame Arresters
This standard is issued under the fixed designation F3386/F3386M; the number immediately following the designation indicates the year
of original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval.
A superscript epsilon (´) indicates an editorial change since the last revision or reapproval.
1. Scope*
1.1 This specification provides the minimum requirements for design, construction, performance, and testing of detonation flame
arresters intended to protect against deflagrations, overdriven (unstable) detonations, stable detonations, and stabilized burning.
1.2 This specification is intended for detonation flame arresters installed in vapor control systems at Marine Facilities subject to
the requirements in 33 CFR, Part 154, Subpart P — Marine Vapor Control Systems.
NOTE 1—In 1990, by permission from ASTM International, an earlier draft of this specification was incorporated and printed in 33 CFR, Part 154,
Appendix A.
1.3 This specification is intended for detonation flame arresters protecting systems containing gases or vapors of liquids with flash
points 140°F [60°C] (closed cup) or less. The tests in this specification are intended to qualify detonation flame arresters for all
in-line applications, provided the operating pressure is equal to or less than the maximum operating pressure determined by testing
and stated in the manufacturer’s certification, and the diameter of the piping system in which the detonation flame arrester is to
be installed is equal to or less than the piping diameter used in the testing.
1.4 This specification is limited to detonation flame arresters operating at temperatures no greater than 140°F [60°C], unless the
detonation flame arresters are tested at the higher operating temperatures.
NOTE 2—Refer to UL 525 for additional requirements that may be applicable.
1.5 The values stated in either SI units or inch-pound units are to be regarded separately as standard. The values stated in each
system are not necessarily exact equivalents; therefore, to ensure conformance with the standard, each system shall be used
independently of the other, and values from the two systems shall not be combined.
1.6 This standard does not purport to address all of the safety concerns, if any, associated with its use. It is the responsibility
of the user of this standard to establish appropriate safety, health, and environmental practices and determine the applicability of
regulatory limitations prior to use.
1.7 This international standard was developed in accordance with internationally recognized principles on standardization
established in the Decision on Principles for the Development of International Standards, Guides and Recommendations issued
by the World Trade Organization Technical Barriers to Trade (TBT) Committee.
This specification is under the jurisdiction of ASTM Committee F25 on Ships and Marine Technology and is the direct responsibility of Subcommittee F25.11 on
Machinery and Piping Systems.
Current edition approved July 1, 2020May 1, 2021. Published July 2020June 2021. Originally approved in 2019. Last previous edition approved in 20192020 as
F3386/F3386M – 19.20. DOI: 10.1520/F3386_F3386M-20.10.1520/F3386_F3386M-21.
*A Summary of Changes section appears at the end of this standard
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United States
F3386/F3386M − 21
2. Referenced Documents
2.1 ASTM Standards:
A395/A395M Specification for Ferritic Ductile Iron Pressure-Retaining Castings for Use at Elevated Temperatures
F722 Specification for Welded Joints for Shipboard Piping Systems
F1155 Practice for Selection and Application of Piping System Materials
2.2 ASME Standards:
ASME B16.5 Pipe Flanges and Flanged Fittings: NPS 1/2 through NPS 24 Metric/Inch Standard
ASME Boiler and Pressure Vessel Code Section VIII,
Division 1
ASME Boiler and Pressure Vessel Code Section IX
2.3 Code of Federal Regulations (CFR):
Title 33, Part 154 Facilities Transferring Oil or Hazardous Material in Bulk
2.4 UL Standards:
UL 525 Standard for Flame Arresters
2.5 Other Documents:
International Electrotechnical Commission: 60079-20-1 Explosive Atmospheres – Part 20-1: Material Characteristics for Gas
and Vapour Classification – Test Methods and Data
3. Terminology
3.1 Definitions:
3.1.1 ΔP/P , n—the dimensionless ratio, for any deflagration and detonation test in 9.3, of the maximum pressure increase (the
o
maximum pressure minus the initial pressure), as measured in the piping system on the side of the detonation flame arrester where
ignition begins by the device described in 9.3.3, to the initial absolute pressure in, P , the piping system.
o
3.1.1.1 Discussion—
The initial pressure should be greater than or equal to the maximum operating pressure specified in 11.1.6.
3.1.2 deflagration, n—a combustion wave that propagates subsonically (as measured at the pressure and temperature of the flame
front) by the transfer of heat and active chemical species to the unburned gas ahead of the flame front.
3.1.3 detonation, n—a reaction in a combustion wave propagating at sonic or supersonic (as measured at the pressure and
temperature of the flame front) velocity and characterized by a shock wave.
3.1.3.1 Discussion—
A detonation is stable when it has no significant variation of velocity and pressure or may be unstable during the transition of a
combustion process from a deflagration into a stable detonation. The transition occurs in a limited spatial zone, where the velocity
of the combustion wave is not constant and where the explosion pressure is significantly higher than in a stable detonation. When
a deflagration transitions to a detonation, it must pass through the overdriven or unstable phase before becoming stable.
3.1.4 detonation flame arrester, n—a device which prevents the transmission of a detonation and a deflagration.
3.1.5 flame passage, n—the transmission of a flame through a device.
3.1.6 flame speed, n—the speed at which a flame propagates along a pipe or other system.
3.1.7 gasoline vapors, n—a non-leaded petroleum distillate consisting essentially of aliphatic hydrocarbon compounds with a
boiling range approximating 149 to 167°F [65 to 75°C].
3.1.8 marine facility, n—a facility as defined in 33 CFR, Part 154.
For referenced ASTM standards, visit the ASTM website, www.astm.org, or contact ASTM Customer Service at service@astm.org. For Annual Book of ASTM Standards
volume information, refer to the standard’s Document Summary page on the ASTM website.
Available from American Society of Mechanical Engineers (ASME), ASME International Headquarters, Two Park Ave., New York, NY 10016-5990, http://
www.asme.org.
Available from U.S. Government Printing Office, Superintendent of Documents, 732 N. Capitol St., NW, Washington, DC 20401-0001, http://www.access.gpo.gov.
Available from Underwriters Laboratories (UL), UL Headquarters, 333 Pfingsten Road, Northbrook, IL, 60062, http://www.ul.com.
Available from International Electrotechnical Commission (IEC), 3, rue de Varembé, 1st floor, P.O. Box 131, CH-1211, Geneva 20, Switzerland, https://www.iec.ch.
F3386/F3386M − 21
3.1.9 maximum experimental safe gap (MESG), n—the maximum clearance between two parallel metal surfaces that has been
found, under specified test conditions, to prevent an explosion in a test chamber from being propagated to a secondary chamber
containing the same gas or vapor at the same concentration.
4. Classification
4.1 The two types of detonation flame arresters covered in this specification are classified as follows:
4.1.1 Type I—Detonation flame arresters acceptable for applications where stationary flames may rest on the device.
4.1.2 Type II—Detonation flame arresters acceptable for applications where stationary flames are unlikely to rest on the device,
and further methods are provided to prevent flame passage when a stationary flame occurs. One example of “further methods” is
a temperature monitor which activates a fire safe automatic shutoff valve.
5. Ordering Information
5.1 Orders for detonation flame arresters under this specification shall include the following information as applicable:
5.1.1 Type (I or II),
5.1.2 Nominal pipe size,
5.1.3 Each gas or vapor in the system and the corresponding MESG,
5.1.4 Inspection and tests other than in addition to those specified by this standard,
5.1.5 Anticipated ambient air temperature range,
5.1.6 Purchaser’s inspection requirements (see 10.1),
5.1.7 Description of installation,
5.1.8 Materials of construction (see Section 6),
5.1.9 Maximum flow rate and the maximum design pressure drop for that maximum flow rate, and
5.1.10 Maximum operating pressure.
6. Materials
6.1 The detonation flame arrester housing, and other parts or bolting used for pressure retention, shall be constructed of materials
listed in Practice F1155, or Section VIII, Division 1, of the ASME Boiler and Pressure Vessel Code. Cast and malleable iron shall
not be used; however, ductile cast iron in accordance with Specification A395/A395M may be used.
6.2 Detonation flame arresters, elements, gaskets, and seals must be made of materials resistant to attack by seawater and the
liquids and vapors contained in the system being protected (see 5.1.3).
6.3 Nonmetallic materials, other than gaskets and seals, shall not be used in the construction of pressure-retaining components of
the detonation flame arrester.
6.4 Nonmetallic gaskets and seals shall be non-combustible and suitable for the service intended.
6.5 Bolting materials, other than those in 6.1, shall be at least equal to those listed in Table 1 of ASME B16.5.
6.6 The possibility of galvanic corrosion shall be considered in the selection of materials.
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6.7 All other parts shall be constructed of materials suitable for the service intended.
7. Other Requirements
7.1 Detonation flame arrester housings shall be gas-tight to prevent the escape of vapors.
7.2 Detonation flame arrester elements shall fit in the housing in a manner that will ensure tightness of metal-to-metal contacts
in such a way that flame cannot pass between the element and the housing.
7.2.1 The net free area through detonation flame arrester elements shall be at least 1.5 times the cross-sectional area of the arrester
inlet.
7.3 Housings, elements, and seal gasket materials shall be capable of withstanding the maximum and minimum pressures and
temperatures to which the device may be exposed under both normal and the specified fire test conditions in Section 9 and shall
be capable of withstanding the corrosion test in 8.2.2, the hydrostatic pressure test in 8.2.3, the pneumatic test in 8.2.10, and the
production tests in 10.3.
7.4 Threaded or flanged pipe connections shall comply with the applicable ASME B16 standards in accordance with Practice
F1155. Welded joints shall comply with Specification F722.
7.5 All flat joints of the housing shall be machined true and shall provide for a joint having adequate metal-to-metal contact.
7.6 Where welded construction is used for pressure-retaining components, welded joint design details, welding and non-
destructive testing shall be in accordance with Section VIII, Division 1, of the ASME Code and Specification F722. Welders and
weld procedures shall be qualified in accordance with Section IX of the ASME Code.
7.7 The design of detonation flame arresters shall allow for ease of inspection and removal of internal elements if necessary, for
such operation as cleaning, repair or replacement.
7.8 Detonation flame arresters shall allow for efficient drainage of condensate without impairing their efficiency to prevent the
passage of flame. The housing may be fitted with one or more drain plugs for this purpose. The design of a drain plug shall be
such that by cursory visual inspection it is obvious whether the drain was left open.
7.9 All fastenings shall be protected against loosening.
7.10 Detonation flame arresters shall be designed and constructed to minimize the effect of fouling under normal operating
conditions.
7.11 Detonation flame arresters shall be capable of operating over the full range of ambient air temperatures anticipated.
7.12 Detonation flame arresters shall be of first class workmanship and free from imperfections which may affect their intended
purpose.
7.13 Detonation flame arresters shall be tested in accordance with the tests described in Section 8.
8. Prototype Tests
8.1 Tests shall be conducted by an independent laboratory capable of performing the tests. The manufacturer, in choosing a
laboratory, accepts that it is a qualified independent laboratory by determining that it has (or has access to) the apparatus, facilities,
personnel, and calibrated instruments that are necessary to test detonation flame arresters in accordance with this specification.
8.1.1 A test report shall be prepared by the laboratory which shall include:
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8.1.1.1 Detailed drawings of the detonation flame arrester and its components (including a parts list identifying the materials of
construction).
8.1.1.2 Types of tests conducted and results obtained. This shall include the maximum temperature reached and the length of
testing time in 9.2 in the case of Type II detonation flame arresters.
8.1.1.3 Description of approved attachments (see 8.2.7).
8.1.1.4 Types of gases or vapors for which the detonation flame arrester is approved.
8.1.1.5 Drawings of the test rig.
8.1.1.6 Initial test pressure and test temperature.
8.1.1.7 Record of all markings found on the tested detonation flame arrester.
8.1.1.8 A report number.
8.2 One of each model Type I and Type II detonation flame arrester shall be tested. Where approval of more than one size of a
detonation flame arrester design series is desired, only the largest, smallest, and one intermediate size of the design series need be
tested provided it is demonstrated by calculation or other testing, or both, that the other intermediate size devices have equal or
greater strength to withstand the force of a detonation and have equivalent detonation arresting characteristics. A change of design,
material, or construction which may affect the corrosion resistance or ability to resist endurance burning, deflagrations or
detonations shall be considered a change of model for the purpose of this paragraph.
8.2.1 The detonation flame arrester shall have the same dimensions, configuration, and most unfavorable clearances expected in
production units. If a test device is modified during the test program, the testing shall be started over again.
8.2.2 A corrosion test shall be conducted. In this test, a complete detonation flame arrester, including a section of pipe similar to
that to which it will be fitted, shall be exposed to a 20 % sodium chloride solution spray at a temperature of 77°F [25°C] for a
period of 240 h and allowed to dry for 48 h. Following this exposure, all movable parts shall operate properly and there shall be
no corrosion deposits which cannot be washed off.
8.2.3 The detonation flame arrester shall be subjected to a hydrostatic pressure test of at least 350 psig [2.4 MPa] for 10 min
without rupturing, leaking, or showing permanent distortion.
8.2.4 Flow characteristics as declared by the manufacturer shall be demonstrated by appropriate tests.
8.2.5 Detonation flame arresters shall be subjected to tests for deflagration, detonation, and endurance burn, in accordance with
the test procedures in Section 9. The same detonation flame arrester shall be used for all tests. Detonation flame arresters designed
to operate at pressures other than atmospheric shall be tested at a pressure equal to or greater than the upper limit of the device’s
maximum operating pressure (see 11.1.6). Type I detonation flame arresters shall show no flame passage when subjected to all three
tests. Type II detonation flame arresters shall show no evidence of flame passage during the detonation/deflagration tests in 9.3.
Type II detonation flame arresters shall be tested for endurance burn in accordance with 9.2. From the endurance burn test of a
Type II detonation flame arrester, the maximum temperature reached and the test duration shall be recorded and provided as part
of the laboratory test report.
8.2.6 When tested in accordance with Section 9, detonation flame arresters shall prevent the transmission of flame and detonation
flame arrester housings shall be able to withstand, without damage or permanent deformation, the internal pressure and
temperatures resulting from both stable and overdriven (unstable) detonations and endurance burning.
8.2.7 Where a detonation flame arrester is provided with cowls, weather hoods and deflectors, etc., it shall be tested in each
configuration in which it is provided.
8.2.8 Detonation flame arresters which are provided with a heating arrangement shall pass the required tests with the heating
arrangement installed and operating at the maximum heated operating temperature.
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8.2.9 Detonation flame arresters designed for operating at temperatures greater than 140°F [60°C], shall be tested at temperatures
greater than or equal to the maximum operating temperature.
8.2.10 After completing all other required tests, each detonation arrester shall be pneumatically tested at 10 psig [70 kPa] for 10
min to ensure there is no leakage.
9. Test Procedures for Detonation Flame Arresters
9.1 Media/Air Mixtures:
9.1.1 For detonation flame arresters intended for use with vapors
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