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The significance of IP inspection in
a ‘zero-defect’ PIMS
• Significance of the POF specification
• Creation of certainty
• Corrosion growth (assumption)
• Risk assessment and IP inspection
• IP tool selection
Hugo van Merrienboer - TAQA Energy
Netherlands
Remnant life prediction
• Operations window  relevant degradation
mechanism (corrosion, erosion, fatigue,
mechanical damages, etc)
• Degradation features, morphology &
dimensions
• POD of the degradation features by (IP)
inspection
• Accuracy, precision & certainty of sizing
Hugo van Merrienboer - TAQA Energy
Netherlands
Ingredients of remnant life prediction
• Time depending growth information
• Probabilistic approach including uncertainties
• Informatin of (internal) operations window
• Information of external interferences
• Pipe material mechanical properties
(statistical distributions)
• Effectiveness Cathodic Protection
• Risk evaluation and acceptance method
Hugo van Merrienboer - TAQA Energy
Netherlands
IP Inspection &
Remnant Life Prediction ?
you know you don't know
what you know what you know
IP Results (POD) Additional (uncertainty) analyses
The unpredictables !
you know you don't know
what you what you don't know
don't know ' Sword fishes & Elephants'
(1 - POD) Leakage !!
The need of (additional) analyses
Hugo van Merrienboer - TAQA Energy
Netherlands
Why ?
Hugo van Merrienboer - TAQA Energy
Netherlands
Know what you know & don’t know 
POF specification
• Standardized variation of defect morphology
• POD per defect morphology
• Statistics: Precision and Accuracy
• XL spreadsheet presentation
Hugo van Merrienboer - TAQA Energy
Netherlands
Standardized defect morphology(example DMR IP Technique)
DMR
TEPNL H. van Merriënboer & A. Suurmond
EXP / MIN Seminar – April 2008
Hugo van Merrienboer - TAQA Energy
Netherlands
Probabilty of Detection (POD)
Hugo van Merrienboer - TAQA Energy
Netherlands
POF – probabilistic validation
Hugo van Merrienboer - TAQA Energy
Netherlands
Defect size correction
Hugo van Merrienboer - TAQA Energy
Netherlands
Zero Defect Approach – Remnant Life Prediction
• Probabilistic correction of defect dimensions
• Corrosion growth estimation/modelling
• Implementation in pressure failure models
(preferably BS/DNV  Tensile strength)
• Failure modes: PH, Hole and Rupture
• PH leakage is serious failure mode !!
Hugo van Merrienboer - TAQA Energy
Netherlands
Example – 12”x 11,5 mm pipe line, Pdesign 101 bar, natural gas.
Corrected defect dimensions at 99% confidence
Hugo van Merrienboer - TAQA Energy
Netherlands
Corrosion growth estimated from largest defect depth
Hugo van Merrienboer - TAQA Energy
Netherlands
Example Pitting
Hugo van Merrienboer - TAQA Energy
Netherlands
Know what you know and know what you don’t know!
IP inspection triggers mitigation actions to a remnant life approach
Hugo van Merrienboer - TAQA Energy
Netherlands
Sequential IP runs, Example MFL
and UT
Know what you don't know!!!!
Comparison of sequential IP runs
IP run n IP technique A (MFL)
pipe nr X pipe nr: Xn1 pipe nr: X n2
Run 1
weld n weld n+1
IP log distance M IP run n
IP run n+1 IP Technique B (UT)
pipe nr X pipe nr: Xn1 pipe nr: X n ????
Run 2
weld n weld n+1
same IP log distance M IP run n+1
Line up !
Hugo van Merrienboer - TAQA Energy
Netherlands
Sequential MFL and UT, sizing
correction by POF data
Process of comparison of sequential IP runs:
Step 1 Lining up of girth welds & clock position.
Run 1 & 2 pipe nr X pipe nr: Xn1 pipe nr: X n2
a e h
g
b k
c i
weld n weld n+1
d
IP log distance M IP run n
Step 3 Uncertainty correction at sizing 90% certainty --> 2 x SD MFL --> + d 25% WT UT --> + 0, 5mm WT
L 40 mm L 20 mm
W 40 mm W 20 mm
a
e g
k
b
c h
weld n i weld n+1
d
Step 4 Comparison: probabilistic algoritm - Select a probabilty of a 'hit' A mfl n1 ᴖA ut n2 > 80% g = h i = g c = d k = k a = a
idem > 90% g = h i = g c ≠ d k = k a = a
A = 'surface W x L' at maximum dimensions at ' X' confidence level idem > 95% g = h i ≠ g c ≠ d k = k a = a
idem > 99% e = e h = h i = i g = h i ≠ g c ≠ d e ≠ c i ≠ h k = k a = a
idem > 50% g = h i = g c = d k = k a = a
idem < 50% a = e b = e i = h e = d b = c a = b k ≠ k a ≠ a
Hugo van Merrienboer - TAQA Energy
Netherlands
More complexities: longitudinal
welded versus seamless pipeStep 5 Know what you know!
--> The difference between longitudinal welded and seamless pipe
--> Compare apples and banana's ?
a
e g
k
b
c h
weld n i weld n+1
d
Spiral/Longitudinal welded: accuracy MFL versus UT d nominal
SD MFL = + 5 - 10% WT WT
SD UT = + 0,5 - 1 mm
a
e g Pattern recognision!
---> Use to identify/characterize defects
k
b
c h
weld n i weld n+1
d
Seamless pipe: accuracy MFL versus UT
SD MFL = + 25 - 30% WT Relative
Relative inaccuracy MFL !! (app. 2 - 4 mm).
SD UT = + 0,5-1 mm Absolute
The thinner the pipe the larger the problem!
WT seamless pipe
d nominal --> input for Pf calculation !!!!!
Hugo van Merrienboer - TAQA Energy
Netherlands
Risk Assessment Subsea Pipe Lines – Production loss at
various LOC morphologies (PH, Hole, Rupture)
Hugo van Merrienboer - TAQA Energy
Netherlands
Long term consequence of IP tool selection.
Hugo van Merrienboer - TAQA Energy
Netherlands
Estimation ‘risk business loss’ because of IP tool
selection
Hugo van Merrienboer - TAQA Energy
Netherlands
TAP: H.van Merrienboer - February 2015 (rev.0)
Safety - Integrity Risk Evaluation Matrix
K 506-08 Failure probability Pipe Lines
P f = 1/Km.year = 10 E-n; En = exponent of 10 Suspected pinhole leakage
Safety Effect
Cost
Effect
<
10
E-5
('neverheard
ofit')
10
E-5
<Pf<
10
E-4
('heard
of
in
the
industry')
10
E-4
<
Pf<
10
E-3
('heard
of
once
peryearin
the
industryoronce
atTAQ
A
global')
10
E-3
<Pf<
10
E-2
('hashappened
m
ore
than
once
per
yearatTAQ
A
Global')
>
10
E-2
('hashappened
m
ore
than
once
peryearatTAQA
Netherlands')
M
itigation
Code
Sligth injury ofhealth effect -Not
effecting work performance or daily life
activities - no first aid or medical case
<10 E4
Minor injury or health effect -Effecting
work performance -Work under
restrictions -Take up to five days to fully
recover -Effecting daily life activities up
to 5 days -Reversible health effect -
modified duty/restricted work case - LTI
< 5 days
10 E4 <C <10 E5
3) Section
replacement
forrest crossing
1, 2)Situation 2012:
Certainty after IP
insp & hydr. Test
Situation 2015:
Uncertainty
Corrosion growth
effect ? -Section
crossing dune
forrest
1, 2, 3
Moderate impact -Major injury or health
effect - Effecting work performance > 5
days - Effecting daily life activities >5
days - Inreversible health effect
10 E5 < C <10 E6
Major impact - Up to 3 fatalities and/or
completely disabled and/or
occupational illness
10 E6 <C <10 E7
Massive Impact -More than 3 fatalities >10 E7
Mitigation measures Mitigation Planning/cost
Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description
1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons
2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test.
3 NA >2016/10000Ke NA > 1000 Replacement pipe section
Hugo van Merrienboer - TAQA Energy
Netherlands
TAP: H.van Merrienboer - February 2015 (rev.0)
Busines Loss - Integrity Risk Evaluation Matrix
Failure probability Pipe Lines
P f = 1/Km.year = 10 E-n; En = exponent of 10 Suspected pinhole leakage
Business Cost
Effect
<
10
E-5
('neverheard
ofit')
10
E-5
<Pf<
10
E-4
('heard
of
in
the
industry')
10
E-4
<
Pf<
10
E-3
('heard
of
once
peryearin
the
industryoronce
atTAQ
A
global')
10
E-3
<Pf<
10
E-2
('hashappened
m
ore
than
once
per
yearatTAQ
A
Global')>
10
E-2
('hashappened
m
ore
than
once
peryearatTAQA
Netherlands')
M
itigation
Code
<10 E4
10 E4 <C <10 E5
3) Section
replacement
forrest crossing
1,2 )Situation 2012:
Certainty after IP
insp & hydr. Test
1,2 3
10 E5 <C <10 E6
Situation 2015:
Uncertainty
Corrosion growth
effect ? - Section
crossing dune forrest
10 E6 <C <10 E7
>10 E7
Mitigation measures Mitigation Planning/cost
Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description
1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons
2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test.
3 NA >2016/10000Ke NA > 1000 Replacement pipe section
Hugo van Merrienboer - TAQA Energy
Netherlands
TAP: H.van Merrienboer - February 2015 (rev.0)
Environment - Integrity Risk Evaluation Matrix
Failure probability Pipe Lines
P f = 1/Km.year = 10 E-n; En = exponent of 10 Suspected pinhole leakage
Environmen
tal Effect
Estimated
Cost Effect
<
10
E-5
('neverheard
ofit')
10
E-5
<Pf<
10
E-4
('heard
ofin
the
industry')
10
E-4
<
Pf<
10
E-3
('heard
ofonce
peryearin
the
industry
or
once
atTAQ
A
global')
10
E-3
<Pf<
10
E-2
('hashappened
m
ore
than
once
per
yearatTAQ
A
Global')
>
10
E-2
('hashappened
m
ore
than
once
peryearatTAQA
Netherlands')
M
itigation
Code
Sligth effect - Contained
into premises
<10 E4
Minor effect - Minor
environmental damage, not
lasting
10 E4 <C <10 E5
3) Section
replacement forrest
crossing
1, 2) Situation
2012: Certainty
after IP insp &
hydr. Test
1,2,3
Moderate effect -limited
environmental damage,
that will persist or requires
cleaning up
10 E5 <C <10 E6
Situation 2015:
Uncertainty
Corrosion growth
effect ? -Section
crossing dune
forrest
Major effect - Severe
environmental damage
that requires extensive
measures to restore its
natural properties. Oil spill
ofmore than 100 barrels
10 E6 <C <10 E7
Massive impact -Persistant
severe environmental
damage -(Permanent) loss
ofcommercial, recreational
use or loss of natural
recources over a wide area
>10 E7
Mitigation measures Mitigation Planning/cost
Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description
1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons
2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test.
3 NA >2016/10000Ke NA > 1000 Replacement pipe section
Hugo van Merrienboer - TAQA Energy
Netherlands
TAP: H.van Merrienboer - February 2015 (rev.0)
Reputation/Legislation - Integrity Risk Evaluation Matrix
Failure probabilty Pipe Lines Failure Probability Pipe Lines
P f = 1/Km.year = 10E-n; En = exponent of 10 Suspected pinhole leakage
Reputation/
Legislative
Effect
Estimated
Cost
Effect
<
10
E-5
('neverheard
ofit')
10
E-5
<Pf<
10
E-4
('heard
ofin
the
industry')
10
E-4
<
Pf<
10
E-3
('heard
ofonce
peryearin
the
industry
or
once
atTAQ
A
global')
10
E-3
<Pf<
10
E-2
('hashappened
m
ore
than
once
peryearatTAQA
Global')
>
10
E-2
('hashappened
m
ore
than
once
peryearatTAQA
Netherlands')M
itigation
Code
Slight impact - Remark at
compliance with no legal
effects
<10 E4
1,2 Situation
2012: Certainty
after IP insp &
hydr. Test
1,2
Minor impact - Official
warning
10 E4 <C <10 E5
3) Section
replacement
forrest crossing
3
Moderate impact - Penalty -
Licence to operatie in
danger
10 E5 <C <10 E6
Situation 2015:
Uncertainty
Corrosion growth
effect ? - Section
crossing dune
forrest
Major impact - National
reputation damage - Local
Lost oflicence to operate
10 E6 <C <10 E7
Massive impact -
International reputation
damage - National long
term permit/licence to
operate lost
>10 E7
Mitigation measures Mitigation Planning/cost
Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description
1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons
2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test.
3 NA >2016/10000Ke NA > 1000 Replacement pipe section
Hugo van Merrienboer - TAQA Energy
Netherlands
In summary:
Only probabilistic (risk) analyses migth help.
Most used statistics ('awareness of uncertainties') :
POF: POD, Accuarcy (= Standard Deviation), Precision ( = statistical average)
---> At all defect types: PH, Pitting, Ax Slot, AxG r, Gen, Circ Slot, Ax Slot.
---> At all defects: statistical correction of dimensions at d, L and W.
Additinal Statistical Evaluations:
H0:'depth run 1 = depth run 2'
--> corrosion growth analyses
--> at individual defects and/or at average defect depths
Additional analyses:
longitudinal welded versus seamless
corrosion morphology modelling: f(d) = L^x
remnant life analyses
--> P failure at dimensional corrected defects (PH, Pitting, Gen, etc)
--> P failure at corrosion growth at service years
Consequences of IP tool
--> From Risk Assessment ('Business loss Cost at Remaining Service years')
Make a Business Case of each IP run
--> Presentation IP as mitigation option in Risk Matrix.
---> 'Know what you know' by implementing al the (above) analyse results into your business case!!
The significance of IP inspection
into a ‘zero-defect’ PIMS
Hugo van Merrienboer - TAQA Energy
Netherlands

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HAK IP pres (2).xlsx

  • 1. The significance of IP inspection in a ‘zero-defect’ PIMS • Significance of the POF specification • Creation of certainty • Corrosion growth (assumption) • Risk assessment and IP inspection • IP tool selection Hugo van Merrienboer - TAQA Energy Netherlands
  • 2. Remnant life prediction • Operations window  relevant degradation mechanism (corrosion, erosion, fatigue, mechanical damages, etc) • Degradation features, morphology & dimensions • POD of the degradation features by (IP) inspection • Accuracy, precision & certainty of sizing Hugo van Merrienboer - TAQA Energy Netherlands
  • 3. Ingredients of remnant life prediction • Time depending growth information • Probabilistic approach including uncertainties • Informatin of (internal) operations window • Information of external interferences • Pipe material mechanical properties (statistical distributions) • Effectiveness Cathodic Protection • Risk evaluation and acceptance method Hugo van Merrienboer - TAQA Energy Netherlands
  • 4. IP Inspection & Remnant Life Prediction ? you know you don't know what you know what you know IP Results (POD) Additional (uncertainty) analyses The unpredictables ! you know you don't know what you what you don't know don't know ' Sword fishes & Elephants' (1 - POD) Leakage !! The need of (additional) analyses Hugo van Merrienboer - TAQA Energy Netherlands
  • 5. Why ? Hugo van Merrienboer - TAQA Energy Netherlands
  • 6. Know what you know & don’t know  POF specification • Standardized variation of defect morphology • POD per defect morphology • Statistics: Precision and Accuracy • XL spreadsheet presentation Hugo van Merrienboer - TAQA Energy Netherlands
  • 7. Standardized defect morphology(example DMR IP Technique) DMR TEPNL H. van Merriënboer & A. Suurmond EXP / MIN Seminar – April 2008 Hugo van Merrienboer - TAQA Energy Netherlands
  • 8. Probabilty of Detection (POD) Hugo van Merrienboer - TAQA Energy Netherlands
  • 9. POF – probabilistic validation Hugo van Merrienboer - TAQA Energy Netherlands
  • 10. Defect size correction Hugo van Merrienboer - TAQA Energy Netherlands
  • 11. Zero Defect Approach – Remnant Life Prediction • Probabilistic correction of defect dimensions • Corrosion growth estimation/modelling • Implementation in pressure failure models (preferably BS/DNV  Tensile strength) • Failure modes: PH, Hole and Rupture • PH leakage is serious failure mode !! Hugo van Merrienboer - TAQA Energy Netherlands
  • 12. Example – 12”x 11,5 mm pipe line, Pdesign 101 bar, natural gas. Corrected defect dimensions at 99% confidence Hugo van Merrienboer - TAQA Energy Netherlands
  • 13. Corrosion growth estimated from largest defect depth Hugo van Merrienboer - TAQA Energy Netherlands
  • 14. Example Pitting Hugo van Merrienboer - TAQA Energy Netherlands
  • 15. Know what you know and know what you don’t know! IP inspection triggers mitigation actions to a remnant life approach Hugo van Merrienboer - TAQA Energy Netherlands
  • 16. Sequential IP runs, Example MFL and UT Know what you don't know!!!! Comparison of sequential IP runs IP run n IP technique A (MFL) pipe nr X pipe nr: Xn1 pipe nr: X n2 Run 1 weld n weld n+1 IP log distance M IP run n IP run n+1 IP Technique B (UT) pipe nr X pipe nr: Xn1 pipe nr: X n ???? Run 2 weld n weld n+1 same IP log distance M IP run n+1 Line up ! Hugo van Merrienboer - TAQA Energy Netherlands
  • 17. Sequential MFL and UT, sizing correction by POF data Process of comparison of sequential IP runs: Step 1 Lining up of girth welds & clock position. Run 1 & 2 pipe nr X pipe nr: Xn1 pipe nr: X n2 a e h g b k c i weld n weld n+1 d IP log distance M IP run n Step 3 Uncertainty correction at sizing 90% certainty --> 2 x SD MFL --> + d 25% WT UT --> + 0, 5mm WT L 40 mm L 20 mm W 40 mm W 20 mm a e g k b c h weld n i weld n+1 d Step 4 Comparison: probabilistic algoritm - Select a probabilty of a 'hit' A mfl n1 ᴖA ut n2 > 80% g = h i = g c = d k = k a = a idem > 90% g = h i = g c ≠ d k = k a = a A = 'surface W x L' at maximum dimensions at ' X' confidence level idem > 95% g = h i ≠ g c ≠ d k = k a = a idem > 99% e = e h = h i = i g = h i ≠ g c ≠ d e ≠ c i ≠ h k = k a = a idem > 50% g = h i = g c = d k = k a = a idem < 50% a = e b = e i = h e = d b = c a = b k ≠ k a ≠ a Hugo van Merrienboer - TAQA Energy Netherlands
  • 18. More complexities: longitudinal welded versus seamless pipeStep 5 Know what you know! --> The difference between longitudinal welded and seamless pipe --> Compare apples and banana's ? a e g k b c h weld n i weld n+1 d Spiral/Longitudinal welded: accuracy MFL versus UT d nominal SD MFL = + 5 - 10% WT WT SD UT = + 0,5 - 1 mm a e g Pattern recognision! ---> Use to identify/characterize defects k b c h weld n i weld n+1 d Seamless pipe: accuracy MFL versus UT SD MFL = + 25 - 30% WT Relative Relative inaccuracy MFL !! (app. 2 - 4 mm). SD UT = + 0,5-1 mm Absolute The thinner the pipe the larger the problem! WT seamless pipe d nominal --> input for Pf calculation !!!!! Hugo van Merrienboer - TAQA Energy Netherlands
  • 19. Risk Assessment Subsea Pipe Lines – Production loss at various LOC morphologies (PH, Hole, Rupture) Hugo van Merrienboer - TAQA Energy Netherlands
  • 20. Long term consequence of IP tool selection. Hugo van Merrienboer - TAQA Energy Netherlands
  • 21. Estimation ‘risk business loss’ because of IP tool selection Hugo van Merrienboer - TAQA Energy Netherlands
  • 22. TAP: H.van Merrienboer - February 2015 (rev.0) Safety - Integrity Risk Evaluation Matrix K 506-08 Failure probability Pipe Lines P f = 1/Km.year = 10 E-n; En = exponent of 10 Suspected pinhole leakage Safety Effect Cost Effect < 10 E-5 ('neverheard ofit') 10 E-5 <Pf< 10 E-4 ('heard of in the industry') 10 E-4 < Pf< 10 E-3 ('heard of once peryearin the industryoronce atTAQ A global') 10 E-3 <Pf< 10 E-2 ('hashappened m ore than once per yearatTAQ A Global') > 10 E-2 ('hashappened m ore than once peryearatTAQA Netherlands') M itigation Code Sligth injury ofhealth effect -Not effecting work performance or daily life activities - no first aid or medical case <10 E4 Minor injury or health effect -Effecting work performance -Work under restrictions -Take up to five days to fully recover -Effecting daily life activities up to 5 days -Reversible health effect - modified duty/restricted work case - LTI < 5 days 10 E4 <C <10 E5 3) Section replacement forrest crossing 1, 2)Situation 2012: Certainty after IP insp & hydr. Test Situation 2015: Uncertainty Corrosion growth effect ? -Section crossing dune forrest 1, 2, 3 Moderate impact -Major injury or health effect - Effecting work performance > 5 days - Effecting daily life activities >5 days - Inreversible health effect 10 E5 < C <10 E6 Major impact - Up to 3 fatalities and/or completely disabled and/or occupational illness 10 E6 <C <10 E7 Massive Impact -More than 3 fatalities >10 E7 Mitigation measures Mitigation Planning/cost Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description 1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons 2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test. 3 NA >2016/10000Ke NA > 1000 Replacement pipe section Hugo van Merrienboer - TAQA Energy Netherlands
  • 23. TAP: H.van Merrienboer - February 2015 (rev.0) Busines Loss - Integrity Risk Evaluation Matrix Failure probability Pipe Lines P f = 1/Km.year = 10 E-n; En = exponent of 10 Suspected pinhole leakage Business Cost Effect < 10 E-5 ('neverheard ofit') 10 E-5 <Pf< 10 E-4 ('heard of in the industry') 10 E-4 < Pf< 10 E-3 ('heard of once peryearin the industryoronce atTAQ A global') 10 E-3 <Pf< 10 E-2 ('hashappened m ore than once per yearatTAQ A Global')> 10 E-2 ('hashappened m ore than once peryearatTAQA Netherlands') M itigation Code <10 E4 10 E4 <C <10 E5 3) Section replacement forrest crossing 1,2 )Situation 2012: Certainty after IP insp & hydr. Test 1,2 3 10 E5 <C <10 E6 Situation 2015: Uncertainty Corrosion growth effect ? - Section crossing dune forrest 10 E6 <C <10 E7 >10 E7 Mitigation measures Mitigation Planning/cost Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description 1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons 2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test. 3 NA >2016/10000Ke NA > 1000 Replacement pipe section Hugo van Merrienboer - TAQA Energy Netherlands
  • 24. TAP: H.van Merrienboer - February 2015 (rev.0) Environment - Integrity Risk Evaluation Matrix Failure probability Pipe Lines P f = 1/Km.year = 10 E-n; En = exponent of 10 Suspected pinhole leakage Environmen tal Effect Estimated Cost Effect < 10 E-5 ('neverheard ofit') 10 E-5 <Pf< 10 E-4 ('heard ofin the industry') 10 E-4 < Pf< 10 E-3 ('heard ofonce peryearin the industry or once atTAQ A global') 10 E-3 <Pf< 10 E-2 ('hashappened m ore than once per yearatTAQ A Global') > 10 E-2 ('hashappened m ore than once peryearatTAQA Netherlands') M itigation Code Sligth effect - Contained into premises <10 E4 Minor effect - Minor environmental damage, not lasting 10 E4 <C <10 E5 3) Section replacement forrest crossing 1, 2) Situation 2012: Certainty after IP insp & hydr. Test 1,2,3 Moderate effect -limited environmental damage, that will persist or requires cleaning up 10 E5 <C <10 E6 Situation 2015: Uncertainty Corrosion growth effect ? -Section crossing dune forrest Major effect - Severe environmental damage that requires extensive measures to restore its natural properties. Oil spill ofmore than 100 barrels 10 E6 <C <10 E7 Massive impact -Persistant severe environmental damage -(Permanent) loss ofcommercial, recreational use or loss of natural recources over a wide area >10 E7 Mitigation measures Mitigation Planning/cost Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description 1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons 2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test. 3 NA >2016/10000Ke NA > 1000 Replacement pipe section Hugo van Merrienboer - TAQA Energy Netherlands
  • 25. TAP: H.van Merrienboer - February 2015 (rev.0) Reputation/Legislation - Integrity Risk Evaluation Matrix Failure probabilty Pipe Lines Failure Probability Pipe Lines P f = 1/Km.year = 10E-n; En = exponent of 10 Suspected pinhole leakage Reputation/ Legislative Effect Estimated Cost Effect < 10 E-5 ('neverheard ofit') 10 E-5 <Pf< 10 E-4 ('heard ofin the industry') 10 E-4 < Pf< 10 E-3 ('heard ofonce peryearin the industry or once atTAQ A global') 10 E-3 <Pf< 10 E-2 ('hashappened m ore than once peryearatTAQA Global') > 10 E-2 ('hashappened m ore than once peryearatTAQA Netherlands')M itigation Code Slight impact - Remark at compliance with no legal effects <10 E4 1,2 Situation 2012: Certainty after IP insp & hydr. Test 1,2 Minor impact - Official warning 10 E4 <C <10 E5 3) Section replacement forrest crossing 3 Moderate impact - Penalty - Licence to operatie in danger 10 E5 <C <10 E6 Situation 2015: Uncertainty Corrosion growth effect ? - Section crossing dune forrest Major impact - National reputation damage - Local Lost oflicence to operate 10 E6 <C <10 E7 Massive impact - International reputation damage - National long term permit/licence to operate lost >10 E7 Mitigation measures Mitigation Planning/cost Code year/cost year/cost year/cost Cost Magnitude (Kϵ) Description 1 2015/25 Ke >2016/5 Ke 5 Ke/y remnant life > 10 Corr. growth coupons 2 NA NA 2017/200 ke > 100 IP inspection, excl. hydr.test. 3 NA >2016/10000Ke NA > 1000 Replacement pipe section Hugo van Merrienboer - TAQA Energy Netherlands
  • 26. In summary: Only probabilistic (risk) analyses migth help. Most used statistics ('awareness of uncertainties') : POF: POD, Accuarcy (= Standard Deviation), Precision ( = statistical average) ---> At all defect types: PH, Pitting, Ax Slot, AxG r, Gen, Circ Slot, Ax Slot. ---> At all defects: statistical correction of dimensions at d, L and W. Additinal Statistical Evaluations: H0:'depth run 1 = depth run 2' --> corrosion growth analyses --> at individual defects and/or at average defect depths Additional analyses: longitudinal welded versus seamless corrosion morphology modelling: f(d) = L^x remnant life analyses --> P failure at dimensional corrected defects (PH, Pitting, Gen, etc) --> P failure at corrosion growth at service years Consequences of IP tool --> From Risk Assessment ('Business loss Cost at Remaining Service years') Make a Business Case of each IP run --> Presentation IP as mitigation option in Risk Matrix. ---> 'Know what you know' by implementing al the (above) analyse results into your business case!! The significance of IP inspection into a ‘zero-defect’ PIMS Hugo van Merrienboer - TAQA Energy Netherlands