# U.S. DOT/PHMSA - Briefing Paper - Internal Corrosion - July 24, 2007

- **operation:** document
- **citation:** 0900006480e8d3eb
- **title:** U.S. DOT/PHMSA - Briefing Paper - Internal Corrosion - July 24, 2007
- **source type:** rulemaking
- **agency:** Pipeline and Hazardous Materials Safety Administration
- **status:** current
- **official:** true
- **published on:** Not available
- **effective on:** Not available
- **summary:** The briefing paper (July 24, 2007) frames a committee discussion to review the adequacy of internal corrosion regulations for hazardous liquid pipelines per Section 22 of the Pipeline Integrity, Protection, and Enforcement Safety Act of 2006. It summarizes current regulatory requirements (§195.579 and §195.452), presents recent risk history and incident statistics (2002–mid‑2007), and lists specific questions for committee consideration regarding acceptability of risk, leak detection, consensus standards, risk control strategies, PHMSA involvement, monitoring decisions following a 2006 BP internal corrosion spill, and guidance on cleaning pigs/corrosion inhibitors and design standards. The document is a discussion/decision paper and poses questions rather than asserting agency conclusions; it cites reported damages and volumes lost from internal corrosion incidents and notes an unregu‑ l
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- **app url:** https://regulus.evalyn.ai/document/regulations-gov-attachment-0900006480e8d3eb
- **source url:** https://downloads.regulations.gov/PHMSA-RSPA-1998-4470-0239/attachment_1.pdf
**body:**

<<<PAGE 1>>>

Briefing Paper July 24, 2007
Technical Hazardous Liquid Pipeline Safety Standards Committee
Adequacy of Internal Corrosion Regulations for Hazardous Liquid Pipelines
Committee action: Discussion.
Contact: Barbara Betsock
Statutory direction: Section 22 of the Pipeline Integrity, Protection, and Enforcement
Safety Act of 2006 directs PHMSA
. . . in consultation with the Technical Hazardous Liquid Pipeline Safety Standards
Committee and other appropriate entities [to] review the internal corrosion control
regulations set forth in subpart H of part 195 of title 49 of the Code of Federal
Regulations to determine if such regulations are currently adequate to ensure that the
pipeline facilities subject to such regulations will not present a hazard to public safety
or the environment.
Current regulations on internal corrosion:
• Section 195.579(a) requires an operator who transports a hazardous liquid that
would corrode the pipeline to take adequate steps to mitigate internal corrosion.
• If an operator uses corrosion inhibitors, an operator must follow § 195.579(b)
which sets requirements for inhibitors and coupons.
• When an operator removes pipe from a pipeline, §195.579(c) requires an operator
to check for internal corrosion.
• If a pipeline’s failure could affect an HCA (commercially navigable waterway,
high population area, other populated area, or unusually sensitive area), the
operator must identify whether internal corrosion is a threat. If it is, § 195.452
requires an operator to have a continual process of evaluation and assessment to
maintain integrity.
Risk history:
• Between 2002 and mid-2007, hazardous liquid pipeline accidents due to internal
corrosion reported to PHMSA resulted in $10.9 million in property damage, and
72.7 thousand lost barrels. Property damage includes damage to the property of
the operator or others, cost of clean-up and recovery, value of lost product. It is
reportable to the extent it exceeds $50,000.
• Slow leaks due to internal corrosion can go undetected for years and pollute
aquifers and soils.
• Based on PHMSA data from the past 5 years, 91% of internal corrosion accidents
on hazardous liquid pipelines occurred on crude pipelines. This includes $7
million of the damages and 67.9 thousand lost barrels.
• An unregulated BP low pressure pipeline failed on March 2, 2006, and spilled an
estimated 201,000 gallons of crude oil onto the tundra on the North Slope of
Alaska near Prudhoe Bay. The cause was internal corrosion. Because the
pipeline is not regulated, the accident is not included in PHMSA data.

<<<PAGE 2>>>

• Is this extent of risk acceptable? Explain why or why not?
• Is leak detection in use on most crude lines sufficient to detect internal corrosion
leaks?
Control of risk:
• What consensus standards or best practices exist on internal corrosion?
• Are these standards/practices adequate forms of risk control?
• Would you use any particular strategy to assign priorities to risk control options?
If so, what might these be?
• Should PHMSA get involved in controlling risks here? If so how (by regulating,
sponsoring best practices workshops, participating in development of consensus
standards, etc.)
• After the BP accident, PHMSA proposed to require low stress pipelines in high
consequence areas to be continually monitored for internal corrosion in a notice of
proposed rulemaking published in September 2006. Because the low stress lines
covered in this first phase of low stress regulation will be covered by the continual
evaluation requirement in integrity management, PHMSA decided to drop the
requirement for continual monitoring for internal corrosion risk. In the
supplemental notice of proposed rulemaking issued in May 2007, PHMSA noted
that it would consider the need for continual monitoring for internal corrosion for
all pipelines (including those operating above 20 percent SMYS) in the second
phase of the rulemaking on low stress lines. How should PHMSA handle this?
• Operators commonly include use of cleaning pigs and corrosion inhibitors as part
of internal corrosion programs. Is there good guidance on this method of control?
If more is needed, what is the best approach?
• The transportation of hazardous liquids poses a greater risk of internal corrosion
than the transportation of natural gas. At the recommendation of the National
Transportation Safety Board, PHMSA adopted design and construction standards
addressing internal corrosion in gas transmission pipelines. (72 FR 20055, April
23, 2007). Is there good guidance for hazardous liquid pipelines? If more is
needed, what is the best approach?
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