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ASTM F1973-99e2

(Specification)

Standard Specification for Factory Assebled Anodeless Risers and Transition Fittings in Polyethylene (PE) Fuel Gas Distribution Systems

Standard Specification for Factory Assebled Anodeless Risers and Transition Fittings in Polyethylene (PE) Fuel Gas Distribution Systems

SCOPE
1.1 This specification covers requirements and test methods for the qualification of factory assembled anodeless risers and transition fittings, in sizes through NPS 8, for use in polyethylene (PE) gas distribution systems.
1.2 The test methods described are not intended to be routine quality control tests.
1.3 The values given in parentheses are for informational purposes only.
1.4 Throughout this specification footnotes are provided for informational purposes and shall not be considered as requirements of this specification.

General Information

Status
Historical
Publication Date
09-May-1999
ICS
75.200 - Petroleum products and natural gas handling equipment
Technical Committee
F17 - Plastic Piping Systems
Drafting Committee
F17.60 - Gas
Current Stage
Ref Project

Relations

Replaces
ASTM F1973-99e1 - Standard Specification for Factory Assembled Anodeless Risers and Transition Fittings in Polyethylene (PE) Fuel Gas Distribution Systems
Effective Date
10-May-1999
Replaced By
ASTM F1973-02 - Standard Specification for Factory Assembled Anodeless Risers and Transition Fittings in Polyethylene (PE) and Polyamide 11 (PA11) Fuel Gas Distribution Systems
Effective Date
10-Sep-2002
Referred By
ASTM F412-23 - Standard Terminology Relating to Plastic Piping Systems
Effective Date
10-May-1999
Referred By
ASTM F3524/F3524M-23 - Standard Specification for Polyamide-12 (PA12) Line Pipe
Effective Date
10-May-1999
Referred By
ASTM F2785-21 - Standard Specification for Polyamide 12 Gas Pressure Pipe, Tubing, and Fittings
Effective Date
10-May-1999
Referred By
ASTM F2619/F2619M-20 - Standard Specification for High-Density Polyethylene (PE) Line Pipe
Effective Date
10-May-1999
Referred By
ASTM F2945-18 - Standard Specification for Polyamide 11 Gas Pressure Pipe, Tubing, and Fittings
Effective Date
10-May-1999

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ASTM F1973-99e2 - Standard Specification for Factory Assebled Anodeless Risers and Transition Fittings in Polyethylene (PE) Fuel Gas Distribution SystemsASTM F1973-99e2 - Standard Specification for Factory Assebled Anodeless Risers and Transition Fittings in Polyethylene (PE) Fuel Gas Distribution Systems
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ASTM F1973-99e2 - Standard Specification for Factory Assebled Anodeless Risers and Transition Fittings in Polyethylene (PE) Fuel Gas Distribution Systems
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Standards Content (Sample)

NOTICE: This standard has either been superseded and replaced by a new version or discontinued.
Contact ASTM International (www.astm.org) for the latest information.
An American National Standard
e2
Designation: F 1973 – 99
Standard Specification for
Factory Assembled Anodeless Risers and Transition
1
Fittings in Polyethylene (PE) Fuel Gas Distribution Systems
This standard is issued under the fixed designation F 1973; 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 (e) indicates an editorial change since the last revision or reapproval.
1
e NOTE—Sections 7.4.3 and 7.4.4 were editorially updated in November 2001.
2
e NOTE—Section 9 was editorially updated in December 2002.
1. Scope ANSI B 31.8 Gas Transmission and Distribution Piping
7
Systems
1.1 This specification covers requirements and test methods
ANSI/ASME B1.20.1 Pipe Threads, General Purpose
for the qualification of factory assembled anodeless risers and
7
(inch)
transition fittings, in sizes through NPS 8, for use in polyeth-
7
ANSI B 16.5 Steel Pipe Flanges, Flanged Fittings
ylene (PE) gas distribution systems.
2.4 ASME Standard:
1.2 The test methods described are not intended to be
8
ASME Boiler and Pressure Vessel Code
routine quality control tests.
2.5 API Standard:
1.3 The values given in parentheses are for informational
API 1104 Standard for Welding Pipelines and Related
purposes only.
9
Facilities
1.4 Throughout this specification footnotes are provided for
2.6 UL Standard:
informational purposes and shall not be considered as require-
10
UL 360 Flexible Metal Hose
ments of this specification.
2.7 PPI Standard:
2. Referenced Documents
PPI TR-4 Hydrostatic Design Bases and Maximum Recom-
mended Design Stresses for Thermoplastic Piping Mate-
2.1 ASTM Standards:
11
2
rials
A 53 Specification for Welded and Seamless Steel Pipe
A 513 Specification for Electric-Resistance-Welded Carbon
3. Terminology
2
and Alloy Steel Mechanical Tubing
3
3.1 The gas industry terminology used in this specification
D 638 Test Method for Tensile Property of Plastics
3
is in accordance with ANSI B31.8 or the United States CFR 49
D 1600 Abbreviations of Terms Relating to Plastics
Part 192, unless otherwise indicated.
D 2513 Specification for Thermoplastic Gas Pressure Pipe,
4
3.1.1 The term “pipe” used herein refers to both “pipe” and
Tubing and Fittings
“tubing” unless specifically stated otherwise.
E 515 Test Method for Leaks Using Bubble Emission Tech-
5
3.1.2 The term “gas” used herein refers to any fuel gas
niques
unless specifically stated otherwise.
F 412 Definitions of Terms Relating to Plastic Piping Sys-
4
3.2 Definitions—Definitions are in accordance with Defini-
tems
tions F 412 unless otherwise specified. Abbreviations are in
F 1588 Test Method for Constant Tensile Load Joint Test
4
accordance with Abbreviations D 1600 unless otherwise speci-
(CTLJT)
fied.
2.2 US Government Document:
3.2.1 anodeless flex riser casing—a flexible, plastic coated,
United States Code of Federal Regulations Title 49 Part
6 metallic, non-gas carrying, protective outer sleeve portion of an
192
2.3 ANSI Standards:
7
Available from American National Standards Institute, 11 W. 42nd St., 13th
1
This specification is under the jurisdiction of ASTM Committee F-17 on Plastic Floor, New York, NY 10036.
8
Piping Systems and is the direct responsibility of Subcommittee F17.60 on Gas. Available from ASME, Three Park Ave., Codes & Standards, New York, NY
Current edition approved May 10, 1999. Published August 1999. 10016.
2 9
Annual Book of ASTM Standards, Vol 01.01. Available from American Petroleum Institute, 1220 L St., NW, Washington, DC
3
Annual Book of ASTM Standards, Vol 08.01. 20005.
4 10
Annual Book of ASTM Standards, Vol 08.04. Available from Underwriters Laboratories, 333 Pfingsten Rd., Northbrook, IL
5
Annual Book of ASTM Standards, Vol 03.03. 60062.
6 11
Available from Superintendent of Documents, US Government Printing Office, Available from Plastics Pipe Institute, Inc., 1825 Connecticut Ave., NW, Suite
Washington, DC 20402. 680, Washington, DC 20009.
Copyright © ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.
1

---------------------- Page: 1 ----------------------
NOTICE: This standard has either been superseded and replaced by a new version or discontinued.
Contact ASTM International (www.astm.org) for the latest information.
e2
F1973–99
anodeless riser which is sometimes selected as an alternate to
f = the design (derating) factor for thermoplastic fuel gas
D
rigid riser casings.
piping as set by the authority having jurisdiction. In
3.2.2 anodeless riser—a type of transition fitting which is the United States the design factor is cited in CFR
Title 49 Part 192.121.
designed to transport gas from an underground polyethylene
service line to above-ground st
...

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4.1 This guide may be used in the investigation of underground storage tank systems for equipment problems in a wide variety of applications. Use of this guide is voluntary. It is intended to assist users who want to investigate equipment failures, malfunctions, and other potential causes of suspected releases.  
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5.1 LPG samples can change composition during storage and use from preferential vaporization of lighter (lower molecular weight) hydrocarbon components, dissolved inert gases (N2, Ar, He, and so forth) and other dissolved gases/liquids (NH3, CO2, H2S, H2O, etc.). Careful selection of cylinder type, cylinder volume, and use of inert gas for pressurizing cylinders is required to ensure that composition changes are small enough to maintain the integrity of LPG when used as a QC reference material for various LPG test methods.  
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1.2.1 Modification of the pressure relief (QCC1) valve on single access port cylinders may prohibit the collection or transport of cylinders outside of permitted facilities such as refineries, gas plants or pipeline stations. No modification is generally required for multi-port mower/forklift cylinders that have a separate access port for pressure relief and additional access ports for filling, liquid/vapor withdrawal or liquid level indication. Consult the Authority having Jurisdiction for detailed regional regulatory requirements for transport of LPG in pressurized cylinders.  
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5.1 Selection of corrosion inhibitor for oil field and refinery applications involves qualification of corrosion inhibitors in the laboratory (see Guide G170). Field conditions should be simulated in the laboratory in a fast and cost-effective manner (1).3  
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5.3 The RCE is a compact and relatively inexpensive approach to obtaining varying hydrodynamic conditions in a laboratory apparatus. It allows electrochemical methods of estimating corrosion rates on the specimen and produces a uniform hydrodynamic state across the metal test surface. (2-21)  
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Standard Practice for Evaluating and Qualifying Oil Field and Refinery Corrosion Inhibitors Using Rotating Cage

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5.1 Selection of corrosion inhibitor for oil field and refinery applications involves qualification of corrosion inhibitors in the laboratory (see Guide G170). Field conditions should be simulated in the laboratory in a fast and cost-effective manner (1).3  
5.2 Oil field corrosion inhibitors should provide protection over a range of flow conditions from stagnant to that found during typical production conditions. Not all inhibitors are equally effective over this range of conditions so it is important for a proper evaluation of inhibitors to test the inhibitors using a range of flow conditions.  
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ASTM E3225-20(Practice)
Standard Practice for Performing a Liquid Test of Spill Prevention Equipment and Containment Sumps Used for Interstitial Monitoring of Piping by Visual Examination

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5.1 Periodic testing of spill prevention equipment and containment sumps used for interstitial monitoring of piping is required by US EPA regulation § 40 CFR §280.35.  
5.2 The spill prevention equipment and containment sumps used for interstitial monitoring of piping must be tested at least once every three years to ensure the equipment is liquid tight by using vacuum, pressure, or liquid testing according to § 40 CFR §280.35. Under this practice, an annual test is required.  
5.3 The phrase liquid tight is an ambiguous expression with the acceptable leak rate dependent upon the nature of the liquid and the purpose of the evaluated material. This practice defines liquid tight.  
5.3.1 There is no minimum containment capacity or leak rate criteria for spill prevention equipment or containment sumps used for interstitial monitoring of piping.  
5.4 Spill prevention equipment and containment sumps are designed to contain a regulated substance that is released from the primary fuel path of a UST system including leaks that occur when the delivery hose is disconnected from the fill pipe, until the regulated substance is detected and removed. There is no established maximum leak rate, capacity requirement or holding time.  
5.5 Spill prevention equipment and containment sumps must be properly installed pursuant to § 40 CFR §280.20 in accordance with a code of practice developed by a nationally recognized association or independent testing laboratory and in accordance with the manufacturer's instructions. Properly installed spill prevention equipment and containment sumps will perform as designed unless one or more components have become compromised. Indications of component compromise that could impact the capability of a sump to remain liquid tight are visually observable.  
5.6 This practice is used to perform a liquid test of sumps to determine if the sumps are liquid tight, capable of containing a regulated substance leaked from the primary fuel path of the UST...
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1.1 Spill prevention equipment, and containment sumps are tested periodically to ensure the equipment is liquid tight by using vacuum, pressure, or liquid testing pursuant to United States of America federal regulations found in § 40 CFR 280.35.  
1.2 This practice provides a liquid test by visual examination conducted by a professional inspector to determine if the spill prevention equipment and containment sumps are liquid tight.  
1.3 The user is expected to have knowledge of UST installation procedures and UST operational, maintenance and testing requirements of § 40 CFR 280 et seq, related to the tasks performed.  
1.4 Section 6 provides the minimum qualifications and educational requirements of a professional inspector. The authority having jurisdiction may have additional certification requirements.  
1.5 This practice offers a set of instructions for performing one or more specific operations. This document cannot replace education or experience and should be used in conjunction with professional judgment. Not all aspects of this practice may be applicable in all circumstances. This ASTM standard is not intended to represent or replace the standard of care by which the adequacy of a given professional service must be judged, nor should this document be applied without consideration of a project’s many unique aspects. The word “Standard” in the title means only that the document has been approved through the ASTM consensus process.  
1.6 The values stated in SI units are to be regarded as standard. No other units of measurement are included in this standard.  
1.7 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. Hazards known to this practice are identified in Sec...

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SCOPE
1.1 This specification provides the minimum requirements for the design, fabrication, pressure rating, marking, and testing for fuel oil meters (volumetric positive displacement type).  
1.2 The values stated in inch-pound units are to be regarded as standard. The values given in parentheses are mathematical conversions to SI units that are provided for information only and are not considered standard.  
1.3 The following safety hazards caveat pertains only to the test method section of this specification.  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.  
1.4 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.

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