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    In-Service Inspection and IntegrityAssessment of Above-Ground

    Storage TanksDr. Athanasios Anastasopoulos

    Presentation forTank Storage ConferenceISTANBUL 3 & 4 November 2010

    www.envirocoustics.gr, [email protected], Tel.: (+30) 210-2846801, Fax: (+30) 210-2846805

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    OVERVIEW

    FAILURE OF TIME-BASED MAINTENANCE & NEEDS FOR ONSTREAM INSPECTION

    TANKPACTM : IN SERVICE CONDITION MONITORING FOR TANKFLOORS: Acoustic Emission Tank Floor Testing Overview

    Case Studies

    Validation and Verification

    TALRUTTM: IN-SERVICE CRITICAL ZONE EXAMINATION

    LSI TANK SHELL CORROSION AND WEAR MAPPING

    PCMS: PLANT CONDITION MONITORING & RISK BASEDINSPECTION SOFTWARE

    DISCUSSION AND CONCLUSIONS

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    Failure of time-based maintenanceHot oil tank, 140C: Internally

    inspected 12 months prior to

    failure, including UT+MFL. This

    collapse was due to a narrowband of annular ring corrosion.

    When the ring split the very

    rapid loss of hot liquid pulled a

    vacuum collapsing the tankshell.

    Naphtha Tank: Leaking 100 cubic meters

    per day through a 1cm hole. Operations

    noticed losses after a week, but no visible

    product, which was disappearing intoground. When the plates were cut the

    cavity under the floor was several cubic

    metres in size.

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    Failures of time-based maintenance

    Many more examples.

    Tanks removed from service, cleaned,sludge dumped, tank inspected...and norepairs required..

    Tanks inspected though leaks not alwaysprevented

    If time based internal inspectionworked. this would not behappening....

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    Tank Floors are the only structural part of a tank

    with no access for inspection during operation Access to tank floors for inspection is difficult and costly.

    Leakage is no longer environmentally acceptable.

    Risk of catastrophic failure with severe annular ring damage. Cleaning costs can be >$200,000, + environmental waste

    problem. If no repairs are required these costs are wasted.

    Requirements:

    To identify tanks which do NOT yet require internal inspectionand repair, this prevents the waste of maintenance resourcesand protects the environment.

    To determine the relative condition of damaged floors so that acorrect priority for internal maintenance may be set.

    To do the above with as little disruption to operations aspossible.

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    TANKPAC: IN SERVICE CONDITION

    MONITORING FOR TANK FLOORS

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    AE sensor

    Tank

    AEInstrument

    AE Van

    Acoustic Emission Tank Floor Testing Overview

    AE Sensors (in the Low Ultrasonic Range to

    avoid Interference) mounted on tank wall 1-2m above knuckle

    3-30 sensors per row used depending upon

    size / 1 or 2 rows

    Cables go to test instrumentation

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    Acoustic Sources detectedCorrosion of steel causes

    Acoustic Emission (Yuyama,

    Condello etc).Sources detected by sensors on

    the outside of the tank.

    Spalling of corrosion products.

    Leak noise: (flow interruption, orturbulence).

    External Interference - noise to befiltered:

    Roof movement noise, Structuralmovement, External and pipe-bornenoise, Condensation, Particleimpacts, Valve leakage.

    Signal amplitude >>

    ^ Number of emissions

    time

    Shown above: one hour of emission from a

    tank with very severe corrosion, characteristics

    of emission change with scaling.

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    Time (s)

    mptu

    e

    Htrae

    AE data analysis

    Bottomplate

    AE sensorLiquid bornwave

    AEsource

    Acoustic Emission Tank Floor Testing Overview

    The tank is monitored in service, following conditioning (Valves closed, heaters

    off, agitators off), for a pre-determined time (6-24 hours in advance of test)

    The data is processed to eliminate unwanted sources of noise,

    Location of 3+hit sources by triangulation.

    The data is evaluated against TANKPAC Technology (database, special

    algorithms for location, Correlations, etc.)

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    TANKPACTM: CONDITION MONITORING FOR TANK FLOORS

    Tank floor top view with

    locations of corrosion and/or

    leak sources

    3D plots of located

    corrosion and leak

    sources

    Separate analysis and

    grading of the most

    severe corrosion sites

    100% FLOOR INSPECTION & ANNULAR RING

    Overall Tank Grading, from A (no damage) to E (severe damage), indicate the general

    condition of the Floor.Potential Leak Sites Identified & Graded indicating concentrated sources of severe

    corrosion or leak.

    Combination of Overall Grading with Potential Leak Result in Composite RBI compatible

    Matrix .

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    Recommendations Matrix

    Overall Grade A B C D E

    PLD Grade I I II (n/a) (n/a) (n/a-doesnt occur)

    1 I I II (n/a) (n/a) I > ~4-5 years

    2 I I II II (n/a) II > ~2 years

    3 II II III III III III ~ 1 year*

    4 II III III IV IV IV ~ 0.5 years*

    5 III III IV IV IV *or schedule for internal inspection

    Clearly leaking tanks often unable to grade, (should be opened anyway).

    Active concentrated sources in all data will also increase severity of grading.

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    Corrosion of Internal Zinc Anodes

    Emission reaching three sensors

    is located.

    Internal sacrificial anodes corrode

    in place of tank floor.

    Zinc blocks can be large.

    Oilfield production tanks use

    sacrificial anodes-very active when

    has coating failed, until zinc used,

    then floor corrodes.

    Special procedures used to

    separate anode corrosion from

    floor corrosion.

    Emission from active anodes in a 55

    metre tank, 2m x1m in size, (30 in

    tank, 4/10/16)

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    150 Diameter, Gasoline

    ALL DATA

    TANK -PAC

    GRADE

    A

    B

    C

    D

    E

    North

    Channel 1

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    TANKPAC: In-Service Floor Plate

    Corrosion Assessment

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    3-D view of an E grade crude tank

    and damage found

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    Leaking Tanks Cases

    Gasoline Tank

    Very concentrated source:scale usually 50!

    Doesnt show on tank plot, onepixel. On product tanks smallleaks are not easily identified,except by high concentration.

    ~1mm hole found whenopened.

    Naphtha Tank

    100 cu.m/day loss

    No visible indication of a leak

    Faint smell only

    TANKPACTM test at 2% sensitivitydue to noise - 2 minutesacquisition only:

    1cm hole found at location shown

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    NEW TANK LEAKING

    DEFECTS IN THE

    WELDS.......LEAK

    TANKPACTM:/ LEAK DETECTION

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    Limitations(see method statement)

    Detects and grades active corrosion only.

    Not suitable for assessing the internal condition of tanks which arecleaned mechanically or chemically as this resets the condition,

    (underside OK). Use history!!

    Small leaks may be masked by active floor corrosion.

    Large leaks will mask overall floor condition.

    Activity from active corrosion under insulation may mask floorcondition.

    Location may degrade on very active D/E tanks due tosimultaneous sources, (the tank needs opening anyway!).

    Not all tanks can be tested, due to noise/condensation etc.

    Complex procedure requires extensive training + control.

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    TANKPACTM: VERIFIED RELIABILITY

    1. TANPAC Tests All around the word (Europe, Middle East, Africa, SouthAmerica, Asia and Far East, North America)

    2. PAC TANKPAC Procedure adopted by SAUDI

    ARAMCO.3. PAC TANKPAC Procedure adopted by DOW

    CHEMICALS

    4. PAC TANKPAC Procedure verified by Shell GlobalSolutions (results presented in ECNDT 98)

    5. 1999 EEMUA recommendations to members (1996 Usergroup became part of EEMUA, ~30 Cos -Engineering Equipment Material Users Association- experience now

    >600 tank floor tests, feedback on internal inspection of >150 tanks, procedure at rev.4.)

    6. French Petroleum Institute: UNION FRANCAISE DES INDUSTRIESPETROLIERS (API), Guide Pour Linspection Et La Maintenance Des Reservoirs Mettaliques Aeriens

    Cylindriques Verticaux D Hydrocarbures Liquides En Raffinerie, ANNEXE: Recommandations pour lutilization de

    lemission acoustique a la verification de l etancheite et a levaluation de l activite des corrosion des reservoirs

    verticaux aeriens, Edition Aug. 2000, Paris

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    Comparison with

    Subsequent Inspection

    From correlation of TANKPACTM results withinternal inspection and repairs carried out:

    100% of A-grade tanks - no repairs ordamage to floor

    56% of C-grade tanks - patch repairs

    52% of E-grade tanks - floor replaced

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    Reliability: TANKPACTM

    overall grading vs. repairs required*

    0

    20

    40

    60

    80

    100

    120

    A B C D E

    FU 1/2 Minimal damage: no repairsFU 3 Damage: some repairs

    FU 4 Significant damage: major repair/new floor

    R

    elative(%)

    AE-grade

    Follow-up results versus AE-grades, normalised per AE-grade

    population of 157 tanks (Shell, Dow-Stade, DSM, PKE, Total and PAL database)

    * P.van de Loo/Shell, B.Hermann/Dow, ECNDT 1998

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    Overall AE Grade vs. % of Tanks for crude

    and product tanks from Major Sites

    0

    10

    20

    30

    40

    50

    A B C D E

    %CRUDE

    %PROD.

    %ALL

    ALL SITES IN SURVEY% of tanks

    TANKPAC

    GRADE

    sample size 598 tanks 6/96

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    TANKPAC is a maintenance planning tool

    Significant money savings: No moneywasted for opening of good tanks.

    Maintenance prioritisation: The mostseverely damaged tanks are programmed

    for internal inspection first. Prevention of environmental losses:Earlyidentification of potential leaks.

    Very fast, low-cost inspection withminimal interruption of operations

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    TALRUT

    In-Service Floor Plate

    (Critical Zone)Assessment

    Inspects critical area,~30cm in.

    Automated UT, Plan image.

    40 m/day.

    Indicative, notquantitative.

    Detects first edge ofcorrosion.

    Detects at 30-50%.

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    TALRUT Annular Ring Test

    Left - Example of Indications from a calibration plate (topof plate is the wall tank shell), Right area withoutindications and close up of the respective A-Scan at

    cursor position

    SHELL:

    PLAN VIEW IMAGE SHOWING

    SEVERE UNDERSIDE CORROSION:

    Summary ReportingExample

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    Shell Corrosion

    Surveys Utilizing LSI

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    LSI Tank Shell Corrosion

    And Wear Mapping 18 meter x 500 mm strip:

    10 x2 mm resolution 45 minutes

    scan time (5 min/2m). 450,000 readings.

    Typically: North, South, East, West(drive around above rings).

    Larger tanks add NE, SE, SW, NW Preferential HAZ corrosion and

    local thinning by wear

    Limitations:

    Poor surfaces may loose somedata ( but still hugestatistical sample )

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    C-SCAN of TANK SHELL & PROCESSING OF UT DATA

    FFS throughout Composite C-Scan imagereconstruction in Nominal-Caution-Reject coloring

    mode

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    PCMS & RBI TANKREPORTER S/W

    Mistras TANKREPORTER and PCMS S/W is usedto enhance reporting and assist assetintegrity management. Capabilities includes3D model of the tank with detail weld seamlocations, nozzle locations, TML locations,repair locations, hyperlinks torecommendations and photos of the defectareas, corrosion rate calculations and RBI.

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    In-Service Inspection, using Modern State of the art techniques,

    Integrated within Plant Condition Monitoring Software (PCMS) and

    Risk Based Inspection lead to reliable Integrity Assessment

    offering:

    Determine the condition of damaged floors so that a correct

    priority for internal maintenance may be set, thus:

    Increased Safety, Availability, Reliability

    Reduce rate and impact of unexpected failures

    Identify tanks which do not require internal inspection and

    repair, thus:

    Reduce the number and duration of tank shutdownReduce scope of routine activities

    Resources prioritized for greatest effect

    Reduce costs

    CONCLUSIONS

    Need to know more about our Group please visit our

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    Thank you for your attention,

    Please let us know

    WHAT ARE YOUR QUESTIONS ?

    Need to know more about our Group, please visit our

    web page:

    http://www.mistrasgroup.com/

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