api 571 damage mechanism questions

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  • 7/22/2019 API 571 DAMAGE MECHANISM QUESTIONS

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    Slide 1

    API 571:CONTENTS

    Now we will look at the last group of damagemechanisms covered by API 571

    These are fairly complicated

    corrosion mechanisms,manyof them related to higher

    temperature and oil/gas

    industry/ refinery applications

    4.2.3 Temper Embrittlement

    4.2.7 Brittle Fracture

    4.2.9 Thermal Fatigue

    4.2.14 Erosion/Erosion-Corrosion

    4.2.16 Mechanical Fatigue

    4.3.2 Atmospheric Corrosion4.3.3 Corrosion Under Insulation (CUI)

    4.3.4 Cooling Water Corrosion

    4.3.5 Boiler Water Condensate Corrosion

    4.4.2 Sulfidation

    4.5.1 Chloride Stress Corrosion Cracking (Cl-SCC)

    4.5.2 Corrosion Fatigue

    4.5.3 Caustic SCC (Caustic Embrittlement)

    5.1.2.3 Wet H2S Damage (Blistering/HIC/SOHIC/SCC)

    5.1.3.1 High Temperature Hydrogen Attack (HTHA

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    Slide 2

    REMEMBER THE WAY THAT API 571

    COVERS EACH OF THE MECHANISMS

    Description/appearance

    of the

    damage mechanism

    Critical

    factors

    AffectedequipmentPrevention/

    mitigation

    Inspection/

    monitoring

    Related

    mechanisms

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    Slide 3

    SULFIDATION

    This is a high temperature corrosion mechanism

    Carbon and alloy steels

    Sulphur compounds

    High temperatures

    (260 degC +)

    +

    + =Sulfidation corrosion

    WARNING:

    This is a common closed-book exam topic

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    Slide 4

    SULFIDATION

    API EXAMINATIONS NEARLY ALWAYS HAVE

    QUESTIONS ABOUT SULFIDATION

    What is it?

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    Slide 5

    SULFIDATION

    The main problem is caused by H2S (formed by the

    degradation of Sulphur compounds at high temperature)

    Occurs in crude

    plant,cokers,hydroprocessor units,firedheaters etc.anywhere where there

    are high temperature sulphur streams

    Sulfidation starts to degrade steels abve

    about 500degF (260 degC)

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    Slide 6

    SULFIDATION

    The susceptibility of steels to Sulfidation is shown inthe McConomy curves shown in API 571

    Watch out for exam questions on this

    As the temperature rises

    above 500 degF,the

    sulfidation corrosionrate goes up

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    Slide 7

    Higher Cr alloys(300-400 series stainless steels)

    may be more resistant to sulfidation corrosion

    MITIGATION

    SULFIDATION

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    Slide 8

    STRESS CORROSION CRACKING

    One of the most common corrosion

    mechanisms

    Prevalent in 300 series austenitic stainlesssteel and high chromium alloys

    Where does the come from?

    Often from residual stresses caused by welding

    316 304

    API terminology also calls it Environmentalassisted cracking

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    Slide 9

    STRESS CORROSION CRACKING

    The stress exposes the grain

    boundaries to corrosion

    Temperature range above 60 degC

    (140 degF) and pH>2

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    Slide 10

    SCC

    Rule of thumb

    In many cases ,SCC is due to

    Chlorides attaching the stainless steelSalt

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    Slide 11

    UT will not show very small SCC cracks

    Neitherwill RT

    SCC CAN BE VERY DIFFICULT TODETECT.ALMOST IMPOSSIBLE IN ITS EARLY

    STAGES

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    Slide 12

    CLASSIC SCC

    BRANCHED CRACKS

    Also known as

    bifurcatedcracks

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    Slide 13

    SCC DETECTED BY PT

    Surface abrasion may be

    needed before PT in order to

    show fine SCC cracks

    Cracks would remain hidden

    without surface abrasion

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    Slide 14

    CAUSTIC

    EMBRITTLEMENTA specialist type of SCC caused by alkaline conditions

    The worst offenders are :

    Sodium Hydroxide (NaOH)

    Caustic Potash (KOH)

    Typically found in H2

    S removal units and acid neutralisation units

    Caustic attack in a heat

    exchanger tubesheet

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    Slide 15

    CAUSTIC EMBRITTLEMENT

    Cracks normally start from the surface of the material

    Look at Fig 4-85 in API 571 showing

    how temperature and NaOH

    concentration affects the susceptibility

    of Carbon steel to NaOH

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    Slide 16

    CORROSION FATIGUE

    Cracks caused by a combination of:

    Corrosion Cyclic loadings+

    These cracks often initiate at pits or under deposits

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    Slide 17Fatigue cracks in corroded area: initiated the failure

    Secondary brittle fracture

    CORROSION FATIGUE

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    Slide 18

    Unlike normal fatigue, there is no endurance limit

    for corrosion-assisted fatigue

    Stress

    S

    CyclesN

    No endurance

    limit

    UTS

    CORROSION FATIGUE

    AN IMPORTANT POINT

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    Slide 19

    WET H2S DAMAGE

    API 571 Sec 5.1.2.3 identifies 4 damage mechanisms

    They affect carbon steels and low alloys steels in wet

    H2S environments

    Hydrogen

    blistering

    Hydrogen induced

    cracking (HIC)

    Stress Oriented

    Hydrogen induced

    cracking (SOHIC)

    Sulfide

    SCC

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    Slide 20

    WET H2S DAMAGE

    The type of wet H2S damage that occurs is related tothese factors(see 570 Sec 5.1.2.3..3.)

    pH

    The H2S level presentTemperature

    Hardness

    Type of steel

    PWHT (an important one)

    The actual damage mechanism for all 4

    categories is the permeation of the H2 into the

    materials grain boundariesThis weakens the material and

    causes failure

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    Slide 21

    WET H2S DAMAGE

    Hydrogen blistering

    The Hydrogen is liberated from corrosion

    (not the process fluid)

    It weakens the material structure causing a

    blister (and eventual failure)

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    Slide 22

    WET H2S DAMAGE

    HIC

    Sometimes called stepwise cracking as

    hydrogen causes cracks in the structure

    The cracks weaken the structure and cause failure)

    Can be worse

    near a weld

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    Slide 23

    WET H2S DAMAGE

    SOHIC

    A type of HIC in which the cracks are made

    worse by stress concentrations

    Stress Oriented Hydrogen induced

    cracking (SOHIC)

    Occurs inHAZ at weld

    toes

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    Slide 24

    WET H2S DAMAGE

    Sulfide SCC

    Essentially ..SCC made worse by thepresence of water and H2S

    Can appear in areas of high hardness (e.g. in welds)

    Weld preheat and PWHT

    can help reduce the risk

    (depending on the alloy)

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    Slide 25

    HIGH TEMPERATURE

    HYDROGEN ATTACK(HTHA)

    This is a specialist and complex corrosion mechanism

    In simple terms:At high temperatures,H2 reacts

    with the Carbon in the steel

    forming Ch4 (Methane)

    The resulting loss of Carbides

    weakens the steel

    Fissures start to form,and

    propagate into cracks

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    Slide 26

    Thick-walled tube

    failure

    A neat rectangular section

    is blown out without

    any bulging

    HTHA has attacked the grain

    boundaries

    HTHA TUBE FAILURE

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    Slide 27

    API 571 SUMMARY

    In these 3 presentations we have looked at all of the

    mechanisms in API 571 that are in the API 510 exam syllabus

    Now finish off the module text

    and try the test questions

    NEXT STEP4.2.3 Temper Embrittlement4.2.7 Brittle Fracture4.2.9 Thermal Fatigue

    4.2.14 Erosion/Erosion-Corrosion

    4.2.16 Mechanical Fatigue

    4.3.2 Atmospheric Corrosion4.3.3 Corrosion Under Insulation (CUI)

    4.3.4 Cooling Water Corrosion

    4.3.5 Boiler Water Condensate Corrosion

    4.4.2 Sulfidation

    4.5.1 Chloride Stress Corrosion Cracking (Cl-SCC)

    4.5.2 Corrosion Fatigue4.5.3 Caustic SCC (Caustic Embrittlement)

    5.1.2.3 Wet H2S Damage (Blistering/HIC/SOHIC/SCC)

    5.1.3.1 High Temperature Hydrogen Attack (HTHA