anomaly assessment and repair panel - ingaa
TRANSCRIPT
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Tool Tolerances
October 22nd, 2008Stephen Westwood
Manager New Product DevelopmentBJ Pipeline Inspection Services
Anomaly Assessment and Repair Panel
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Pipe Wall
MFL Tool –
Backing Bar
Magnet Magnet
Brush Brush
Leakage Flux
Sensor Head
Defect
Axial Magnetic Flux Leakage
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MFL Technology
• Inferred Measurement– Not Measuring the Desired Quantity
• Has Limitations– Vendors Aware of– Operators Should be
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Tool Tolerances Why ?
• Wide Range of Shapes, Sizes, WT and Defect Location
• Wide Range of Steel’s
• Line Conditions• Tool Performance• Process Performance
0
5000
10000
15000
20000
25000
0 50 100 150 200 250Magnetic Field H (Oersteds)
Flux
Den
sity
B (G
auss
)
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Tool & Data VerificationPull Rig
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Defect Size (Length, Width, Depth)
Calculating Defect Size
Apply Regression Techniques
Real Corrosion and more...
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Defect Signal & Wall Thickness
Defect Dimensions – 70mm x 70mm x 60%
Wall Thickness – 11.8mm Wall Thickness – 18.6mm
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Velocity Affected Defect2.3m/s – 5.1mph Reported Size
45m x 55mm x 78%
6.8m/s – 15.2mph Reported Size
42mm x 54mm x 40%
Actual Defect Size 45mm x 45mm x 79%
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Real Corrosion ClusterPipe Area
75’’ long
26’’ wide
63 Metal Loss Features
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Communication
• Before Inspection– Threats– Limitations
• During the Inspection– Line Conditions
• After the Inspection– Digs– Feedback
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Significance of ILI Uncertainties
October 22nd, 2008Mark Stephens
Senior ConsultantC-FER Technologies
Anomaly Assessment and Repair Panel
C-FERTechnologies Inc.
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Context for Evaluation
• Reliability– Probability that a prescribed length of the pipeline
will not fail within a certain period of time
– General approach & guidelines developed thru PRCI* provide objective basis for assessing integrity/safety
• Adopted by CSA (Z662 – Annex O)• Under consideration by ASME for inclusion in B31.8
Reliability = 1 – Failure Probability
*Pipeline Research Council International
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Defect Specific Probability Estimation
Data on material properties and
dimensions
Operating pressure
Inspection Data
Inspection-related uncertainties
Burst model and test results
Data from single / multiple
inspections
Failure probability as a
function of time
Model results
Test results
xxxx
xxx
x
xx
x
model uncertainties
Feature dimension
corrosion characteristics
Probability density
Growth Rate
corrosion growth rates
Yield stress
Frequency
pipe properties
Over pressure
Likelihood
load characteristics
Probability density
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ILI Uncertainties
Sources of uncertainty consistent with API 1163
– Probability of detection (POD)• probability of feature being detected
– Probability of false call (POFC)• probability of non-existing feature being reported as feature
– Probability of identification (POI)• probability that detected feature will be corrected identified
– Sizing accuracy (measurement error)• accuracy with which feature dimension is reported
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Key ILI Uncertainties
0
1020
30
4050
60
70
8090
100
0 5 10 15 20 25 30 35 40 45 50
Depth (% wall)
POD
(%)
without detection floorEg: POD = 90% at threshold depth & Threshold depth = 10% wall POD - Basis for inferring density & size distribution of non-detected features
-20 -15 -10 -5 0 5 10 15 20
Error (% wt)
Prob
abili
ty D
ensi
ty
Probability that error is within error band, pint
(confidence level)Mean Error
(bias)
Emin Emax
Error band
minustolerance
in API 1163
plustolerancein API 1163
certainty in API 1163
-20 -15 -10 -5 0 5 10 15 20
Error (% wt)
Prob
abili
ty D
ensi
ty
Probability that error is within error band, pint
(confidence level)Mean Error
(bias)
Emin Emax
Error band
minustolerance
in API 1163
plustolerancein API 1163
certainty in API 1163
minustolerance
in API 1163
plustolerancein API 1163
certainty in API 1163
Tool tolerance & Confidence
Interval – basis for measurement error
distribution
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Comments on Sizing Accuracy
Perfect tool
Actual size Xi
ILI s
ize
Yi
45°
β
Actual size Xi
ILI s
ize
Yi
Real tool - with bias (β) and random error (e)
±e
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Comments on Field Verification
Actual size, Xi
ILI s
ize,
Yi
45°
±e
β
Real tool - with bias (β) and random error (e)
Field size, XiIL
I siz
e, Y
i
45°
±e
β0
β1
Real tool - with bias and random errorcharacterized by field tool with random error and possibly bias
Interpret unity plots with caution!
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Implications for Reliability
*Growth rate - independent of measured defect size
1%
10%
100%
1000%
POD 90% at10%t
Size Error±5%t
Size Error±10%t
Size Error±15%t
Size Error±20%t
Type of Uncertainty
Incr
ease
in P
OF
(rel
ativ
e to
per
fect
tool
)
5 year 10 year 15 year
Class 1 natural gas line 30 NPS @ 940 psi, Grade X60 Hypothetical measured defect population*
Sizing error and impact on reliability estimate
POD and impact on reliability
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Comments on ILI Uncertainties
Impact on reliability• Sources of ILI uncertainty well understood
– Some can conservatively be ignored (e.g. POFC)– Some can have negligible impact (e.g. POD for HR tool*)– Some have more significant impact (e.g. sizing
uncertainty)• Tool performance often better than specified
– Field verification results must be interpreted with caution
*performing to capability for intended features
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Comments on ILI UncertaintiesProcess
– ILI results (interpreted with acknowledgment of inherent uncertainties) inform decisions on what to excavate
– Operators must understand significance of ILI uncertainties
• Verify they are consistent with claims/assumptions
• If not make appropriate adjustmentsTrends
– Technology constantly improving• Tending towards situation where impact of
uncertainties is potentially minimal
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Addressing Corrosion Anomalies as Reported by ILI Tools
October 22nd, 2008Sergio Limon-Tapia
Pipeline Integrity GroupWilliams Gas Pipeline
Anomaly Assessment and Repair Panel
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Outline
• Our Common Goal• The Role of MFL Tools for Addressing Corrosion• Addressing MFL Tool Performance• Elements of an ILI Performance Validation Program• Summary
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Our Common Goal• We all share a common goal: preventing any failures in
the pipelines we manage– Leaks or ruptures– Operators, regulators and ILI providers together
• External Corrosion is one of the primary threats to most pipeline systems– We spend more time, effort and money addressing this threat
• External Corrosion Program– Prevention, control, assessment and mitigation– Stay focused on our normal good practice: CP surveys and
appropriate mitigation responses (ground beds/recoats)– ILI program: an integral part of the corrosion program
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MFL Tools for Addressing Corrosion
• The basic fundamentals of this technology have not changed– Induce a magnetic field that saturates the pipe wall– Coil and Hall sensors capture magnetic flux leakage produced
by the metal loss present– Perform all of these tasks in a single opportunity while traveling
in one direction at about 4-7 MPH• Let’s not forget to recognize and understand the
limitations in the technology– Characterization of various corrosion shapes– Pipeline Operators Forum classification chart– POI, POD specs
• MFL tools, analysts and operators have done a good job in reporting and ranking corrosion features– We need refinement and fine tuning in certain areas
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Addressing MFL Tool Performance
Elements of an ILI Performance Validation Program:• Manage the uncertainties using reliability engineering based
methods– Based on well established statistical & probabilistic principles– Quantify and document the probability of failure of a corroded area as
reported by MFL
• Consider using a form of the Probability of Exceedance concept– The probability that a corrosion feature as reported by MFL exceeds a
threshold level– Determine an acceptable POE threshold level
• Manage integrity using POE/Reliability Engineering– Allows for the prioritization of response and remediation
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Addressing MFL Tool Performance
Elements of an ILI Performance Validation Program: continuation…
• Validate MFL performance– Accurate in-ditch sizing of corrosion is essential– Create depth unity plots and Probability of Failure curves– Provide detailed feedback to the ILI analyst
• Understanding when adjustments to ILI data are needed– Identify correcting factors– Implement adjustments – Document that changes/adjustments made are effective
• Issue a final dig list
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Summary• We all share the common goal to continue to maintain
safety• We have experienced good success with the MFL/Analyst
work in addressing corrosion• MFL tool is an integral part of our corrosion program• The basics of the MFL technology have not changed• We are learning to better handle the uncertainties inherent
in the process (MFL-Analyst-Prioritization-Response- Remediation)
• An ILI performance validation program can be structured using reliability engineering based principles
• The POE approach can assist in quantifying the uncertainness and managing integrity
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Tool Tolerances
October 22nd, 2008Chris Whitney
Manager, Pipeline Services EastEl Paso Pipeline Group
Anomaly Assessment and Repair Panel
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El Paso Pipeline System
• 37,000~ mile system (CIG,EPNG,SNG,TGP)
• 32,000~ miles in ILI program• 3%~ HCA• 60%~ ILI miles to inspect HCAs• 40%~ ILI miles w/o HCA
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EP ILI History
• Pre-2001 – various company approaches– ~10,000 miles, low-resolution
• 2001-2007 (4 Pipes)– 438 segments– 17,800 miles, 14,100 1st time– ~6,500 actionable anomalies remediated
• 2008 – 85 segments, ~4000 miles
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ILI Process
• Deformation and Axial MFL tools• “Clean” Pipeline segment• Tool speed within parameters• Sensors functional – 97% coverage• Tool rotation• Length, data quantity/quality, AGMs, etc.
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ILI Process• Final Report – 60 days• FPR with Modified ASME B31G vs MAOP• Metal loss box interaction• Align data with HCAs• Initial Response report
– Immediate action, pressure restriction– 1 yr dents
• Final Response report– Scheduled investigations
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Tool Tolerance and Uncertainty• HCA
– 70% depth, 1.16 FPR – Immediate Action
• Scheduled Anomalies – Within 2 years of ILI– FPR < 1.39 (10 yr criteria, B31.8S, fig. 4)
• Monitor dig program to confirm expectations– Some unity plots using field reported data– Provide feedback to facilitate improvement and
relationships with vendors.
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Panel 1 Summary• MFL technology is a mature process for metal
loss inspection • Sources of uncertainty are well understood• Various methods are employed to account for
these uncertainties• Operator feedback to ILI providers is critical for
continuous improvement• It is incumbent on Operators to apply
appropriate conservatism to the process• Incident statistics indicate industry is doing a
good job of managing corrosion using all of the tools at our disposal