PHMSA
has posted several updates to the list of frequently asked questions concerning
the Alternative MAOP regulations found under 49 CFR 192.620. The latest
revisions are posted below. To download a complete list of these FAQ’s, go to
the following website: http://primis.phmsa.dot.gov/maop/docsf/faqs.pdf.
1. What is the alternative MAOP Rule?
The alternate MAOP Rule was promulgated by PHMSA to allow certain gas
transmission pipelines to operate at higher pressures and pipeline stress
levels than regulations previously allowed when designed and operated with more
rigorous safety standards. By allowing pipelines to operate at higher pressures
and stress levels, greater efficiencies and gas product throughput can be
achieved (73 FR 62148).
Revised: 9/11/09
11. How will PHMSA handle Special Permit requests to allow pipeline
operation at higher stress levels that were submitted prior to the issuance of
the alternative MAOP Rule?
Formerly pipeline operators were allowed to submit Special Permit requests to
PHMSA to request approval to operate at pressures greater than allowed by the
former regulations. Operators of those pipelines must comply with the final
rule in order to operate their pipelines at a higher alternative MAOP. PHMSA
will examine special permits that have already been granted, as appropriate, to
determine if any modifications are needed.
Revised: 9/11/09
16. Can existing pipelines that have experienced a failure indicative of
materials concerns qualify for the use of a higher alternative MAOP?
49 CFR 192.620 (b) provides for the performance of a root cause analysis to
determine if a failure is indicative of a systemic problem and precludes use of
a higher alternative MAOP only if a failure is determined to be systematic in
nature. Results of the analysis must be reported to regulators (PHMSA Regional
Office or applicable state regulatory authorities).
Revised: 9/11/09
20. How is overpressure protection addressed when operation is at a higher
alternative MAOP?
The alternative MAOP is higher than the upper limit of the required overpressure
protection under previous regulations. 49 CFR 192.620(e) increases the
overpressure protection limit to 104 percent of the MAOP, which is 83.2 percent
of SMYS for a pipeline segment operating at the alternative MAOP in a Class 1
location.
Revised: 9/11/09
23. Why include conditions on plate or coil quality when operating at a
higher alternative MAOP?
All steel pipe is made from either plates or coils. If these steel plates or
coils are of superior quality, then the pipe will also be of superior quality.
Assuring quality requires that the mill that made the plate or coil had an
inspection and quality control program to limit variation and to improve the
quality of its final product – the plate and/or coil. The condition simply
requires that operators verify that such a program was in place at the mill.
Revised: 9/11/09
24. Why are mill test reports required for the Alternate MAOP rule?
The alternate MAOP rule allows operators to establish MAOPs higher than
previously allowed by 49 CFR Part 192. One of the requirements is to have mill
test reports (mechanical and chemical properties) on the steel that went into
the pipe that will operate under the higher stress levels allowed by the
alternate MAOP rule. This requirement was included because PHMSA needs assurance
that the pipe operating at higher stress levels does not to pose a risk to the
integrity of the pipeline. To provide this assurance, an operator must have
documented proof of the actual yield strength, tensile strength, and chemistry
properties of the steel used in the pipe.
Revised: 9/11/09
26. Does the recent advisory bulletin ADB-09-01 (Docket No. PHMSA-2009-0148
– “Potential Low and Variable Yield and Tensile Strength and Chemical
Composition Properties in High Strength Line Pipe”) affect pipelines that
are planned to operate in accordance with the MAOP Rule?
The advisory bulletin informs pipeline system owners and operators of the
potential for high strength line pipe installed in recent pipelines may exhibit
inconsistent chemical and mechanical properties. Yield strength and tensile
strength properties that do not meet the line pipe specification minimums have
been observed. This advisory bulletin pertains to microalloyed high strength
line pipe grades, generally Grade X-70 and above. PHMSA has reviewed
metallurgical testing results from several recent projects indicating pipe
joints produced from plate or coil from the same heat may exhibit variable
chemical and mechanical properties by as much as 15% lower than the reported
strength values by the pipe manufacturer. The advisory bulletin can be obtained
online here.
PHMSA expects operators of pipelines under the alternate MAOP to perform
in-Line Inspections (ILI) that will identify (remove) all threats to the
pipeline. The operator should plan to use a high resolution deformation tool in
lieu of a geometry tool to address the threat described in the Advisory
Bulletin. The deformation tool must include multi-finger sensors and have an
accuracy of +/- 1% to identify expanded pipe and dents.
The results of the initial ILI must be integrated with the initial CIS and
DCVG/ACVG surveys required in accordance with §192.620(d). The operator should
evaluate and repair all anomalies, expanded pipe and dents in accordance with
the MAOP Rule prior to increasing the pressure above the 72% SMYS MAOP to the
alternative MAOP of 80% SMYS for Class 1 locations.
The results of all deformation and geometry tool run results for expanded pipe
and dents should be analyzed and submitted to the PHMSA Regional Director. All
pipe exhibiting an indicated diameter greater than 1.00 % (based upon pipe
diameter) above the nominal pipe diameter should be noted on the report of
potential deformations.
The operator should review with PHMSA Regional Director, the deformation and/or
geometry tool reports. This analysis will consider pipe properties and property
distributions, hydrostatic test pressures and reported test behavior, and pipe
end to center variations. Based on local pressure and expected behavior, any
expansion exceeding anticipated expansion by more than 1.50% may be
investigated by excavation to determine actual expansion and, if necessary, to
verify pipeline special permit segments yield and ultimate tensile strengths,
elongation and chemistry. This guideline may be modified by PHMSA if initial
verification reviews by PHMSA Regional Director show negligible integrity risk.
Revised: 9/11/09
In This Issue
- ANPRM on PHMSA Enforcement of Damage Prevention Laws
- Compliance Management System
- PHMSA Updates FAQ’s for Alternative MAOP Regulations
- PHMSA Adds New Liquid IMP FAQ #12.13
- PHMSA Advisory Committee Meeting – Advance notice
- Standard Operating Procedure Updates
- New Jersey Pipeline Regulations – Misc. Revisions
- Florida Pipeline Safety Regulations – Misc. Proposed Revisions
- Joint Workshop on New Spill Reporting Forms for the Hazardous Liquids Pipeline Industry
- ASME Conference
- Pipeline Regulations for iPhone