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    Leak Detection

    Performance

    Pipeline Safety Trust Conference

    November 17 & 18, 2011

    New rleans, !ouisiana

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    Detection?

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    Why Leak Detection? (Contd)

    Minimize the volume of lost uid

    Reduce risk of re! e"#losion or other safety hazards Protect the com#any

    Minimize cleanu# costs $ith an early res#onse to a leak$arnin%

    Protect re#utation

    Demonstra&le acce#tance of res#onsi&ility &y e"ecutin%a #roactive leak detection #ro%ram

    'l$ays increasin% re%ulatory interest in #i#elineinte%rity #ro%rams includin% leak detection

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference3

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    istory

    Manual #ressure*o$ readin%s and evaluation

    +oice communication &et$een the eld and anycenter of res#onsi&ility that may e"ist! or $ithother stations alon% the line

    ,amiliarity $ith the #i#eline &ehavior &ycontrollers and technicians $as critical

    Ri%ht-of-$ay o&servation includin% $alk-overs andy-overs $ere amon% fe$ leak detection o#tions

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference

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    'utomated Measurements

    Pro#rietary lo%%in% systems and .C'D'

    /ransmitter and meter technolo%y

    'utomation tools and #roducts that ac0uireaccurate information a&out hydraulic &ehavior

    /ools to assist in evaluatin% the relationshi#samon% measurements

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference!

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    Leak Detection

    Performance ,rom the former 'P1 2233 (4valuation Methodolo%y for

    .oft$are 5ased Leak Detection .ystems)6

    /he system correctly indicates that there is no leak

    /he system correctly indicates that there is a leak

    /he system incorrectly indicates that there is a leak(false alarm)

    /he system incorrectly indicates that there is no leak(failure to detect)

    Denitions a&sor&ed into 'P1 RP-2278 (Com#utationalPi#eline Monitorin% for Li0uid Pi#elines)

    November 17 & 18, 2011 Pipeline Safety Trust 2011 Pipeline

    Safety Conference"

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    Performance Metrics

    .ensitivity 9 Com&ination of the size of a

    detecta&le leak and the time re0uired to detect it

    Relia&ility 9 ' measure of the system:s a&ility toaccurately assess $hether a leak e"ists or not

    'ccuracy 9 /he a&ility of a system to estimate leak#arameters such as leak o$ rate! total volumelost! and leak location

    Ro&ustness 9 /he a&ility of a system to continue tofunction durin% unusual hydraulic conditions or$hen data is com#romised

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference7

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    Meter-5ased Leak

    Detection Most $idely used method on lon% haul #i#elines

    Re0uires meters at all entry and e"it #oints

    'chieva&le sensitivity limited &y meter accuracy

    .ome methods can &e im#lemented in .C'D' or areo#tions $ith .C'D' #roducts

    .ome #roducts are stand-alone and driven &y .C'D' data

    'larm thresholds must tolerate and e"#ect the im&alance

    in meter readin%s as the line #acks and un#acks Leak evaluation al%orithms that correlate actual chan%es

    in line#ack $ith meter im&alance #rovide the &est#erformance

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference8

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    'P1 22;< Performance

    Predictions

    Predicts the theoretical &est #erformance #ossi&le

    $ith con%ured uncertainties =o mar%in for false alarm #revention

    /em#erature uncertainty and related chan%es indensity durin% transit is lar%est inuence on#erformance

    =ot uncertainty in measurement! &ut uncertainty intem#erature #role alon% the line

    >ne ty#e of leak detection system can more accuratelyestimate the tem#erature #role than other systems

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference#

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    Denitions

    Dry +olume 9 +olume of the #i#eline at atmos#heric#ressure and a reference tem#erature

    Line#ack 9 /he incremental 0uantity of uid in the linein addition to the dry volume inuenced &y #ressureand uid tem#erature

    Line#ack is heavily inuenced &y tem#erature:s eect onuid density as is #ressure! &ut often to a lesser de%ree

    Prole 9 +alue of a #arameter over the len%th of the#i#eline se%ment

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference10

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    Denitions (cont)

    @ncertainty 9 Potential error in measurements thatmust &e e"#ected and accounted for also the

    de%ree to $hich somethin% is unkno$n and must&e estimated or assumed &ased on some$hatrelated measurementsA

    Real-/ime /ransient Model (R//M) 9 'ccurately

    tracks uid tem#erature*density #roles $ithconsideration of #ressure in order to reduceuncertainty in the line#ack

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference11

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    Meter Buality vsAPerformance

    November 17 & 18, 2011 Pipeline Safety Trust

    2011 Pipeline Safety Conference12

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    Meter-5ased Leak 5asics

    ,lo$*Pressure*/em#erature measurements only at

    se%ment end-#oints

    Metered o$ accuracy im#ortant for hi%h sensitivity

    ,luid density (molecules*mass #er unit volume)

    varies si%nicantly $ith tem#erature Warm uid is less dense Cold uid is more dense

    /em#erature*density #role uncertainty is the mostlimitin% factor in leak detection for some #i#elines

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    +olumetric ,lo$Measurement

    5enets of volumetric (not corrected for tem#erature

    and #ressure) o$ measurement 5arrel-to-&arrel assessment tolerates dierences in

    density at inection and delivery #oints

    /olerates s$itchin% inection sources of dierenttem#eratures

    @seful on short lines $ith small chan%es intem#erature*density durin% transmission

    =ot useful $here tem#erature*density #roles aresi%nicant due to heat loss

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    =et &arrel ,lo$Measurement

    5enets of net (corrected for tem#erature and

    #ressure) o$ measurement @seful for custody transfer

    @nder steady-state conditions! uid inected at lo$erdensity $ill &alance $ith delivered uid at hi%her

    density 1nections at sli%htly hi%her volumetric o$ &alances

    $ith deliveries at lo$er volumetric o$

    'ssumes a sta&le tem#erature*density #role

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    =et ,lo$ Measurement1ssues

    /ransient conditions th$art many al%orithms

    involvin% net o$ measurements Line #ackin% and un#ackin% still result in an a##arent

    net o$ im&alance as $ith &asic volume &alancemethods

    =et &arrel o$ measurements a%%ravate sim#le&alance al%orithms $here a dierence in densitye"ists at inection and delivery #oints e"ce#t understeady-state sta&le conditions

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    =atural ,lo$ 1m&alance

    Dierence in inected uid density and delivered

    uid density radual chan%e in uid density durin% transit

    /em#erature*density #roles are #oorlyunderstood &y most sim#le al%orithms

    Prole chan%es sha#e $ith chan%es in o$ rate

    Water crossin%s and occasionally $et soil increasethermal conductivity

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    Meter-5ased Leak DetectionLimitations

    'ccountin% for chan%es or distur&ances in line#ack

    >#erational chan%es causes the line to #ack orun#ack as a normal occurrence

    .hort-term hydraulic distur&ances (transients)!includin% chan%es in inection tem#eratures! and theireect on line#ack must &e tolerated or understood inshort-term evaluation al%orithms used in ra#idassessments

    >ver e"tended #eriods any eects of transients arediluted thus allo$in% %ood sensitivity &y most meter-&ased solutions over lon% o&servation intervals

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    Eey Conce#ts

    Pressures and tem#eratures under steady-stateconditions #rovide current line#ack characteristics

    Diver%ence of meter readin%s (%reater im&alance) should&e reected in line#ack chan%es as seen in #ressures /ransients distur& this information and can lead to

    si%nicant short-term line#ack uncertainty >ver lon% time intervals any o&served variations in

    line#ack &ecome insi%nicant com#ared to the 0uantity

    of uid #assin% throu%h the #i#eline system Lon%-term sensitivity settin%s do not re0uire as much

    tolerance of line#ack uncertainty as do short term leakdetection thresholds

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    Line#ack 4stimation

    ,luid density assumed to &e an avera%e of inection

    and delivery density Wei%hted avera%e

    Custom al%orithms for curve ttin%

    R//M thermal models track uid density alon% the

    line

    Chan%e in o$ rate alters the tem#erature*density#role as a ne$ 0uiescent state develo#s

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    Proles

    /em#erature

    >ccurs $hen inection and delivery tem#eratures dier

    .u&ect to heat transfer characteristics of environment

    +aries $ith o$ rate * transit time

    Pressure

    +aries as &atched uids of dierent characteristics travel

    +aries as &atches of dierent densities travel over mountains

    Proles are accurately tracked &y Real-/ime /ransientModels

    November 17 & 18, 2011 Pipeline Safety Trust 2011 PipelineSafety Conference

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    Real-/ime /ransient Model

    Most so#histicated volume*mass &alance tool

    1ncludes a thermal model to increase the accuracy of

    line#ack evaluation! thus allo$in% a shorter detection timefor a detecti&le leak

    /racks heat transfer alon% the line and develo#s accuratetem#erature*density #roles as ste# chan%es in o$ rates

    or inection tem#eratures occur

    'llo$s thermal model tunin% to achieve the &est#erformance &y modelin% the hydraulic &ehavior accurately

    'utomatic tunin% ca#a&ilities

    1nstrument sanity checkin%

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    R//M Myths

    .oft$are is e"#ensive

    =ot si%nicantly more e"#ensive

    .oft$are re0uires s#ecial skills /rainin% and full technical su##ort is oered &y vendors

    Eno$led%e of the #i#eline #hysical details is needed

    .oft$are re0uires on%oin% maintenance

    =ot needed! once #erformance is satisfactory! &utfurther tunin% is often #erformed to continually im#rove#erformance

    Re0uired if the #i#eline net$ork is chan%ed

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    .tatic Pressure /estin%

    4"tremely hi%h sensitivity

    Fero (8) o$ results in zero (8) uncertainty in o$measurement

    Works $ell in a relatively incom#ressi&le li0uid

    environment

    Re0uires #ressure control e0ui#ment

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    .tatic Pressure /estin%(contd)

    .hut in under #ressure at near o#eratin% #ressure

    Monitor #ressure decay for a #eriod of time

    Dro# #ressure &y half

    Monitor #ressure decay for a #eriod of time

    ' consistent #ressure decay rate indicates

    decreasin% density due to heat transfer ' dierent #ressure decay rate indicates a leak

    $hose rate is #ressure de#endent

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    .tatic Pressure /est /rends

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    Conclusion

    .im#le line#ack assessment al%orithms have a #lace$here line#ack is sta&le and line#ack variations and

    uncertainty do not adversely aect leak assessment

    R//M technolo%y si%nicantly reduces line#ackuncertainty in transient environments and ena&les leak

    detection a##roachin% the limits im#osed &y meteraccuracy

    .tatic #ressure testin% is a useful inte%rity verication tool

    Matchin% the #ro#er tool to the #i#eline:s o#eration iscritical

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    /rainin% G Res#onse

    ' critical com#onent of any #i#eline inte%rity

    mana%ement #ro%ram Res#onse #rotocol should &e included in trainin% and

    &e enforced Controller can shut do$n the line on any sus#icion of a

    leak

    Details re%ardin% actions! re#ortin%! etcA =o internal #enalty for reasona&le ud%ment

    ' culture focused on #i#eline inte%rity mana%ement iscritical

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    References

    'P1 2278 9 Com#utational Pi#eline Monitorin% for Li0uidPi#elines

    'P1 22;< 9 Pi#eline +aria&le @ncertainties and /heir 4ects onLeak Detecta&ility

    'P1 22H2 9 uidance Document for the Bualication of Pi#elinePersonnel

    ;< C,R Part 2= >, ='/@R'L '=D >/4R'. 5J P1P4L1=46 M1=1M@M ,4D4R'L .',4/J ./'=D'RD.

    ;< C,R Part 2= >, 'F'RD>@. [email protected] P1P4L1=4

    November 17 & 18, 2011 Pipeline Safety Trust2011 Pipeline Safety Conference

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    Contact @/.1

    UTSI - U.S. Headquarters

    23H8 West 5ay 'rea 5oulevard

    .uite 788,riends$ood! /e"as @.' KK3;H

    /ele#hone6 2 I2 ;8KH

    ,a"6 2 I2 ;8 884mail6 infoNutsiAcom

    WWW6 htt#6**$$$AutsiAcom

    Daniel WA =a%ala ([email protected])

    President G C4>

    November 17 & 18, 2011 Pipeline Safety Trust30

    UTSI - EuropeRaimundo ,ernandez +illaverde ;7!

    HL

    I887 Madrid! .#ain

    /ele#hone6 7; (