Abstract

Pneumatic testing is beneficial as an alternative to hydrotesting particularly in remote areas where access to hydrotest fluids becomes logistically difficult or impossible. In some cases, above-ground pipe supports cannot hold the water weight, or that the pipe is coated/lined with materials that would degrade with water/methanol/glycol mixtures, or the system cannot be fully dried and the remaining hydrotest fluids are detrimental to the service application once the system is commissioned. Additionally, the elevation profile of the piping is such that an excessive number of test sections would be required for hydrotesting according to most codes. The present work is aimed at addressing two salient questions often faced with pneumatic testing. The first is related to the appropriate piping volume to consider for calculating the stored energy in use with ASME Post Construction Committee (PCC)-2 calculation for determining the safe exclusion distance for a given piping geometry and test conditions. It was found that the 8D criteria specified in ASME PCC-2 cannot be generalized for all pipe sizes, different material toughness, grades, wall thicknesses, and test conditions. A criterion is developed based on the ductile fracture arrest length that considers all these factors combined. The second criterion is related to the ability to detect a pinhole leak from the pneumatic test data, again for a given geometry and test conditions, and what constitutes the minimum pinhole effective area in relation to the system total volume, measured uncertainties in the test pressure and temperature over the duration of the test. A seminormalized physics-based parameter is suggested that can be applied to determine the effective pinhole leak size. The methodology is applied to a pneumatic field test on DN200, 12.2 km pipeline lateral.

References

1.
ASME, 2018,
Process Piping, ASME Code for Pressure Piping, B31
,” ASME, New York, Standard No. B31.3-2018 (Revision of ASME B31.3-2016).
2.
ASME, 2019, “
Pipeline Transportation Systems for Liquids and Slurries, ASME Code for Pressure Piping, B31
,” ASME, New York, B31.4-2019 (Revision of ASME B31.4-2016).
3.
ASME,
2018, “
Gas Transmission and Distribution Piping Systems, ASME Code for Pressure Piping, B31
,” ASME, New York, Standard No. B31.8-2018 (Revision of ASME B31.8-2016).
4.
U.S. Department of Transportation, 2008, “
Transportation of Natural And Other Gas By Pipeline: Minimum Federal Safety Standards
,” U.S. Department of Transportation, Washington, DC, Standard No.
DOT—49 CFR Ch. I (10–1–11 Edition)
, 192.
5.
U.S. Department of Transportation, 2008, “
Transportation of Hazardous Liquids by Pipeline
,” U.S. Department of Transportation, Washington, DC, Standard No.
DOT- 49 CFR Ch. I (10–1–11 Edition)
, PART 195.
6.
CSA, 2019, “
National Standard of Canada, Oil and Gas Pipeline Systems
,” CSA, Ottawa, ON, Canada, Standard No. Z662:19.
7.
Energy Resources Conservation Board,
2011
, “
Directive 077: Pipelines—Requirements and Reference Tools
,”
Mar. 21, 2011, (updated Dec. 22), Energy Resources Conservation Board, Calgary, AB, Canada.
8.
Australia/New Zeeland Standards, 2021, ANSI Store, Washington, DC, accessed Sept. 28, 2021, https://webstore.ansi.org/standards/sai/nzs28852012
9.
Australia/New Zeeland Standards, 2021, Standards Australia, Sydney, Australia, and Standards New Zealand, Wellington, New Zealand, accessed Sept. 28, 2021, https://www.saiglobal.com/PDFTemp/Previews/OSH/AS/AS3000/3700/3788-2006.pdf
10.
An International Executive Power Secretary Of Environment And Natural Resources Official Mexican Standard, “
Transportation of Natural Gas, Ethane and Gas Associated With Coal Ore Through Pipelines
,” United Mexican States, National Agency of Industrial Safety and Environmental Protection of the Hydrocarbon Sector, Miguel Hidalgo, Mexico, Standard No. NOM-007-ASEA-2016.
11.
ABSA The Pressure Equipment Safety Authority
,
2019
, Standard Pneumatic Test Procedure Requirements for Piping Systems, Edition 2, Revision 2 - Issued 2019-07-31, ABSA The Pressure Equipment Safety Authority, Edmonton, AB, Canada, Standard No. AB-522.
12.
The Pressure Equipment Safety Authority
,
2019
, “Design Registration Requirements for Application-Specific Pneumatic Test Procedures, Edition 1, Revision 1 - Issued 2019-07-31,” The Pressure Equipment Safety Authority, Edmonton, AB, Canada, Standard No. AB–532.
13.
The American Society of Mechanical Engineers (ASME)
,
2018
, “
Repair of Pressure Equipment and Piping PCC-2
,” ASME, New York, Standard.
14.
Ebrahimi
,
K.
, and
Mofrad
,
S. R.
,
2018
, “
Pneumatic Test of Pressurised Equipment: Its Hazards and Alternatives
,”
ASME
Paper No. PVP2018-84025.10.1115/PVP2018-84025
15.
Arti
,
B.
,
Weyer
,
R.
,
Dang
,
T.
, and
Taagepera
,
J.
,
2018
, “
Pneumatic Testing of Piping: Managing the Hazards for High Energy Tests
,”
ASME
Paper No: PVP2018-84078.10.1115/PVP2018-84078
16.
Simpson
,
D. A.
,
2019
, “
Comparative Risks of Hydrostatic and Pneumatic Pipeline Testing
,”
ASME
Paper No. PVP2019-93048.10.1115/PVP2019-93048
17.
Maxey
,
W.
,
Kiefner
,
J. F.
, and
Eiber
,
R. J.
,
1976
, “
Ductile Fracture Arrest in Gas Pipelines
,” American Gas Association, Washington, DC, Catalogue No. L32176.
18.
Eiber
,
R. J.
,
Bubenik
,
T. A.
, and
Maxey
,
W. A.
,
1993
, “
Fracture Control for Natural Gas Pipelines
,” PRCI Report, Pipeline Research Council International, Chantilly, VA, Catalogue No. L51691.
19.
Kunz
,
O.
, and
Wagner
,
W.
,
2012
, “
The GERG-2008 Wide-Range Equation of State for Natural Gases and Other Mixtures: An Expansion of GERG-2004
,”
J. Chem. Eng. Data
,
57
(
11
), pp.
3032
3091
.10.1021/je300655b
20.
Lemmon
,
E. W.
,
Huber
,
M. L.
, and
McLinden
,
M. O.
,
2010
,
NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties - REFPROP, Version 9.0
,
National Institute of Standards and Technology, Standard
,
Gaithersburg
.
21.
Sugie
,
E.
,
Matsuoka
,
M.
,
Akiyama
,
T.
,
Mimura
,
H.
, and
Kawaguchi
,
Y.
,
1982
, “
A Study of Shear Crack Propagation in Gas-Pressurized Pipelines
,”
ASME J. Pressure Vessel Technol.
,
104
(
4
), pp.
338
343
.10.1115/1.3264226
22.
Makino
,
H.
,
Kubo
,
K.
,
Shiwaku
,
T.
,
Endo
,
S.
,
Inoue
,
T.
,
Kawaguchi
,
Y.
,
Matsumoto
,
Y.
, and
Machida
,
S.
,
2001
, “
Prediction for Crack Propagation and Arrest of Shear Fracture in Ultra-High Pressure Nature Gas Pipelines
,”
ISIJ Int.
,
41
(
4
), pp.
381
388
.10.2355/isijinternational.41.381
23.
Makino
,
H.
,
Takeuchi
,
I.
, and
Higuchi
,
R.
,
2008
, “
Fracture Propagation and Arrest in High Pressure Gas Transmission Pipelines by Ultra High Strength Line Pipes
,”
ASME
Paper No. IPC2008-64078.10.1115/IPC2008-64078
24.
Shapiro
,
A. H.
,
1983
,
The Dynamics, and Thermodynamics of Compressible Fluid Flow
, Vol.
1
,
Krieger Publishing Co
,
Malabar, FL
, pp.
972
973
.
25.
Botros
,
K. K.
,
Dunn
,
G. H.
, and
Hrycyk
,
J. A.
, May
1998
, “
Riser - Relief Valve Dynamic Interactions (Extension to a Previous Model)
,”
ASME J. Pressure Vessel Technol.
,
120
(
2
), pp.
207
212
.10.1115/1.2842242
26.
Matta
,
L.
,
2017
, “
Collective Effects of Leakage, Temperature Changes, and Entrapped Air During Hydrostatic Testing
,”
Pipeline Pigging and Integrity Management Conference
, Houston, TX, Mar. 1–2, Paper No. 13.https://www.researchgate.net/publication/314204788_Collective_Effects_of_Leakage_Temperature_Changes_and_Entrapped_Air_During_Hydrostatic_Testing
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