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RAM PIPE REQUAL: A Risk Assessment & Management Based Process for the Requalification of Marine Pipelines Robert Bea Marine Technology & Management Group University of California at Berkeley [email protected]

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  • RAM PIPE REQUAL: A Risk Assessment & Management Based Process for the Requalification of Marine Pipelines

    Robert Bea Marine Technology & Management Group

    University of California at Berkeley [email protected]

    mailto:[email protected]

  • Topics

    RAM PIPE REQUAL

    Reliability Approach

    Level 2 examples: corrosion

    Un-instrumented

    Instrumented

  • RAM PIPE REQUAL Project

    Develop guidelines for requalification of marine pipelines

  • Associated Developments RAM PIPE REQUAL

    Guidelines Project

    RAM PIPE REQUAL special projects

    API RP 1111 LSD SECTION 17

    OTHER ASSOCIATED PROJECTS

    RAM Workshop

    Rosen reliability formulations

    PEMEX requal criteria

    PIMPIS

    PIPE IMR

    Trinidad Pipelines Time Pf's

    DNV RP F 101

    ABS GL

    HSE OTO 99 002

    CFER PIRAMID

  • RAM

    MARINE SYSTEM Design

    Construction

    Decommissioning

    Operation Maintenance

    ASSESSMENT

    MANAGEMENT

    RISK

  • Risk Assessment

    Risks: likelihoods & consequences

    Hazards: uncertainties, threats

    Knowable & unknowable hazards

    Assessment: identify & evaluate

    Alternatives:likelihoods, consequences, both Observe: improve & revise

  • Risk Management

    Alternatives: evaluate, costs, benefits Culture: production & protection

    Identify: alternatives

    Resources: abilities, money, time

    Implementation: plan, organize, lead, control

    Revise: monitor, assess, modify

  • Accidents are caused by people and so are successes

    High Consequence Accidents

    Environment (intrinsic)

    Human (extrinsic)

    80 %

    Design Construction Operations

    80 %

  • Organizations have major influences

    PROPAGATING EVENTS

    Organization Errors - 80 % Other Factors - 20 %

    CONTRIBUTING EVENTS

    Organization Errors - 80 % Other Factors - 20 %

    INITIATING EVENTS

    Individuals errors of: omission - 20 % commission - 80 %

    Near Misses Accidents

  • Primary factors

    Interfaces

    Operators

    Procedures

    HardwareStructure

    Organizations

    Environments

  • REACTIVE empirical

    pproaches frequent accidents

    REAL-TIME PROACTIVE actionpredictive

    frequent andinfrequent infrequentaccidents accidents

    before & after UNSAFE SPACE

    A

  • Three key strategies

    Reduce the likelihood of HOE

    Increase detection & remediation of HOE

    Reduce the effects of HOE

  • Quality, safety, & reliability

    QUALITY ability to satisfy requirements

    Serviceability use for purpose for conditions

    Safety acceptability of risks

    Compatability acceptability of impacts

    Durability freedom from unanticipated

    degradation

  • S T A RT

    S e l e c t P i p e l i n e F o rC o n d i t i o n E v a l u a t eA s s e s s m e n t& S u r v ey R e s u l tsR e q u a l i f i c a t i on

    L E V E L 2 L E V E L 3L E V E L 1 S i m p l i f i e d M e t h o d sQ u a n t i f i e d R i s kS c o r i n g M e t h o d s

    M i x ed A n a l y s i s M e t h o dsQ u a l i t a t i ve

    N e x t C y c le E n g i n e e r N e x tE v a l u a t e A l t e r n a t i v e s I n s p e c t i o n , P i p e l i n e O p e r a t i o n s

    M a i n t e n a n c e , L o a d i n g s M a i n t e n a n c e P r o t e c t i o n I n s p e c t i o n s R e p a i r C y c le

    RAM PIPE REQUAL

  • RAM PIPE REQUAL Level 2 Method Base on physics - mechanics

    Simplified models

    RAM approach

    Performance databases

    Test data verified

    Instrumented & un-instrumented

    Linguistic & quantitative variables

  • Level 2 Burst Capacity Damaged / Defective

    Intact: pB = SU (t / R)

    Corrosion

    pB = (SU / SCFC )(t / R)

    SCFC = 1+2(tc / R)0.5

    R

    t

    tc

  • Pf = P [ Demand (S) " Capacity (R) ]

    .

    R

    p r o b a b i l l i t y

    r e l a t i v e f r e q u e n c y de m and ( S ) o r

    c apac it y ( R)

    S

    Rs t ro n g e r

    p ro p o rt io n a l t o p ro b a b ilit y o f

    f a ilu re ( Pf )

  • Pf

    10 0

    10 -1

    10 -2

    10 -3

    10 -4

    10 -5

    10 -6

    FS 50

    s=0.1 s=0.2 s=0.3 s=0.4

    2 4 6 8 10

  • Nominal Values & Biases

    pB = pO (BpO / BpB ) exp ( b sb s ) = pO B exp ( b s )b s )

    prob

    abili

    ty

    ss B

    B

    Bias = actual / nominal

  • Bia

    s =

    Mea

    sure

    d B

    urst

    Pre

    ssur

    e /

    Com

    pute

    d B

    urst

    Pre

    ssur

    e

    0.4

    0.8

    1.2

    1.6

    2

    .01 .1 1 5 10 2030 50 7080 9095 99 99.999.99 Percent

    http:99.999.99

  • 0.01 0.009 0.008 0.007 0.006 0.005 0.004 0.003 0.002 0.001

    Failu

    re R

    ate

    Gulf of Mexico Pipelines: Pf " 1 to 2 E-3 per year

    0

    oil gas

    8080 8181 8282 8383 8484 8585 8686 8787 8888 8989 9090 9191 9292 9393 9494 9595 9696

    Year

  • Corrosion is the Primary Problem OTHER

    STRUCTURAL3% 6% UNKNOWNNAT.HAZARD

    1%

    CORROSION 47%ERROSION

    MATERIAL 2%

    26% ANCHORING 2%

    4%

    FIRE/EXPLOSION 0%

    IMPACT 8%

    CONSTRUCTION 1%

  • Corrosion Rates from Database

  • Time Dependent Reliability

  • Corrosion: Instrumented 1

    0.8

    0.6

    Prob

    abili

    ty

    0.4

    0.2

    Alyeska Pipeline UK Oil Pipelines

    0.05 0.1 0.15 0.2 0

    Corrosion Rate (mm / year)

    0

  • Probabilities of Detection

  • Measurement Accuracy tC50 = tCD ( BDt ), V tC50 =25 % to 35 %

    Bia

    s =

    1.4

    1.35

    1.3

    1.25

    1.2

    1.15

    1.1

    1.05

    1

    Pig C Pig A

    50 100 150 200 250 300

    Pit Depth (mils)

  • 20-inch gas line instrumented Pig C

    0 5000 10000 15000 Distance (m)

    0.05

    0.1

    0.15

    0.2

    0.25

    0.3

    0.35

    Measured (% t) Corrected (% t)

    Mea

    sure

    d C

    orro

    sion

    (% t)

  • Probabilities of Failure: Detected & Not Detected

    0.01

    0.015

    0.02

    0.025

    0.03

    Prob

    abili

    ty o

    f Fai

    lure

    0 5000 10000 15000 Distance (m)

  • AN

    NU

    AL

    PRO

    BA

    BIL

    ITY

    OF

    INSU

    FFIC

    IEN

    T Q

    UA

    LITY

    Fitness for Purpose1

    0.1

    0.01

    0.001

    0.0001 1 10 1 10 2 10 3

    COST RATIO x PVF

    Marginal

    Optimum

    Bay Campeche pipelines risers

  • Summary RAM PIPE REQUAL approach to

    requalification of pipelines

    Corrosion is the primary problem Need to develop industry database on

    performance of marine pipelines

    RAM PIPE REQUAL project continuing with industrial guidance

  • POP (Performance of Offshore Pipelines) Project

    Pipelines proposed for abandonment

    In-line instrumented and un-instrumented

    Predictions of burst pressures & defects

    Hydrotest pipelines to failure & recover

    Perform material and geometry tests

    Revise predictions Contact James Wiseman at: [email protected]

    mailto:[email protected]

    RAM PIPE REQUAL: A Risk Assessment & Management Based Process for the Requalification of Marine Pipelines Topics RAM PIPE REQUAL Project RAM. Risk Assessment Risk Management Accidents are caused by people. and so are successes Organizations have major influences. Primary factors. Three key strategies Level 2 Method Summary