04 ppp tte api 570 piping inspn

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API 570 Presentation

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    API 570

    PIPING INSPECTION

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    API 570Piping Inspection Code

    570

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    API 570 COVERS IN-SERVICEINSPECTION OF PIPING

    To fit in with the philosophy of ANSI B31.3DESIGN CODE FOR PROCESS PIPING

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    THE SCOPE OF API 570

    Mandatory:Almost anymetallic piping system:Raw and finished oil products

    Raw and finished chemical products

    Hydrogen/fuel/flare gas systemsSour/waste systems etc

    Optional:Water,steam and

    condensate

    Piping related to mechanical

    equipment

    (pumps/compressors etc)

    Pressure vessels

    Domestic sewers etc

    Everything< in dia

    Non-metallic piping

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    API 570 INSPECTION

    PRACTICES

    Checks are needed for specific types of corrosion and cracking:

    1. Injection points

    2. Dead legs

    3. CUI4. Soil /Air(S/A) interfaces

    5. Erosion and erosion/corrosion

    6. SCC

    7. Corrosion under linings

    8. Fatigue cracking9. Creep cracking

    10. Brittle fracture

    11. Freeze damage

    Well look at some of

    these in more detail

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    INJECTION POINTS

    Why is particular inspection attention (and TMLs)needed at

    injection points ?

    .and what are TMLs anyway

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    12in or 3D upstream

    2ndchange of

    flowdirection

    downstream (o

    7.6m after the

    first change)

    INJECTION POINT

    INSPECTION AREAS

    This area is

    known as:The

    IPC(injection

    point circuit)

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    API 570 INSPECTION METHODS

    Internal

    visuals

    TMLs

    (4 quadrants)External

    visual

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    DEADLEGS

    Deadleg

    Corrosion rates are

    higher

    around deadlegs

    Redundant deadlegs

    should be removed

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    CORROSION UNDER

    INSULATION (CUI)

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    CORROSION UNDER

    INSULATION (CUI)

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    CORROSION UNDER

    INSULATION (CUI)

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    CORROSION UNDER

    INSULATION (CUI)

    Almost total wastage

    of bolts

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    CORROSION UNDER INSULATION (CUI)

    API identifies the areas that are most

    susceptible to CUI

    Mist from

    cooling towers

    Near steam vents

    and deluge systems

    Acid vapours

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    AllLCS pipework operating continually at 4

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    CORROSION UNDER FIXED LININGS

    In general ,API does not

    require removal of linings

    for inspectionsAS LONGAS THE L INING IS IN

    GOOD CONDITION

    BUT

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    SOIL/AIR INTERFACES

    All interfaces without cathodic protection

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    The API 570 rule is that you should inspect

    areas for CUI where the insulation is damaged

    CORROSION UNDER

    INSULATION (CUI)

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    RECOMMENDED EXTENT OF CUI

    EXAMINATION(BY CLASS)

    Type of circuit

    % NDT on areas

    with damaged

    insulation

    % NDT on

    suspect areas

    within CUI

    temperature

    range

    Class 1 75% 50%

    Class 2 50% 33%

    Class 3 25% 10%

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    EROSION AND EROSION-CORROSION

    LOCATIONS

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    Control valves (especially when there is flash-off

    Orifice plate

    Pump discharges

    ElbowsPipe features that produce turbulence

    TMLS FOR

    EROSION/CORROSIONDownstream of ..

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    An

    example

    EROSION/CORROSION

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    Erosion/Corrosion

    after flow-restriction

    features

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    STRESS CORROSION

    CRACKING (SCC)

    Rule:

    In most circumstances,SCC is due to

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    SCC ON A GAS PIPELINE

    COMPONENT

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    SCC ON A GAS PIPELINE

    COMPONENT

    Wh t i thi ?

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    What is this?

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    API 570 GUIDE ON REPAIR

    PATCHES

    D

    Max D/2

    Repair patch

    Not permitted

    25mm min radii

    API 570 GUIDE ON REPAIR

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    PATCHES

    Requires a full repair sleeve

    Min 2D

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    API 570 INSPECTION

    INTERVALS

    The maximum permitted interval

    depends on pipe class

    Class 1:Highest risk/consequence

    Class 2: Medium riskClass 3: Low risk

    MAXIMUM API INSPECTION

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    MAXIMUM API INSPECTION

    INTERVALS (BY CLASS)

    Type of circuit Thickness

    measurements

    External visual

    Class 1 5 years 5 years

    Class 2 10 years 5 years

    Class 3 10 years 10 years

    Injection points 3 years By class

    S/A interfaces - By class

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    API 570 PIPING

    CLASSES

    Class 1Flammable services/flash-off leading to brittle fractuExplosive vapours after flash-off

    H2S gaseous

    Hydroflouric acid

    Piping over public roads

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    API 570 PIPING

    CLASSES

    Class 2Most other process piping

    On-site hydrocarbons

    H2, fuel gas and natural gas

    On-site acid and caustics

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    API 570 PIPING CLASSES

    Class 3Fluids that will not flash

    off (even if they are

    flammable)

    Distillate/product

    storage/loading linesOff-site acids and

    caustics

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    API 570 SUMMARY

    API 570 specifies the main points to look for

    Remember the pipe classes (and their inspection

    periods)

    Simple wall thickness determination

    570