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    INSTITUTE OF PHYSICS PUBLISHING JOURNAL OF PHYSICS D: APPLIED PHYSICS

    J. Phys. D: Appl. Phys. 39 (2006) R101R124 doi:10.1088/0022-3727/39/6/R01

    TOPICAL REVIEW

    Elevated temperature erosive wear ofmetallic materials

    Manish Roy

    Defence Metallurgical Research Laboratory, PO Kanchanbagh, Hyderabad 500 258, India

    Received 6 July 2005, in final form 9 December 2005Published 3 March 2006Online at stacks.iop.org/JPhysD/39/R101

    AbstractSolid particle erosion of metals and alloys at elevated temperature isgoverned by the nature of the interaction between erosion and oxidation,which, in turn, is determined by the thickness, pliability, morphology,adhesion characteristics and toughness of the oxide scale. The mainobjective of this paper is to critically review the present state ofunderstanding of the elevated temperature erosion behaviour of metals andalloys. First of all, the erosion testing at elevated temperature is reviewed.This is followed by discussion of the essential features of elevatedtemperature erosion with special emphasis on microscopic observation,giving details of the erosionoxidation (EO) interaction mechanisms. TheEO interaction has been elaborated in the subsequent section. The EOinteraction includes EO maps, analysis of transition criteria from one

    erosion mechanism to another mechanism and quantification of enhancedoxidation kinetics during erosion. Finally, the relevant areas for futurestudies are indicated.

    Nomenclature

    E Erosion rate

    En Erosion rate at nth exposure

    Mn Mass loss suffered due to erosion on nth exposure

    Mn Mass gain experienced due to oxidation on

    nth exposuret Time of exposure to eroding conditions

    mn Cumulative mass of erodent for nth exposure

    V Impact velocity

    K1 Constant

    p Velocity exponent of erosion rate

    Kop Parabolic rate constant

    m Incremental mass gain due to oxidation

    Ao Arrhenius constant

    Q Activation energy for oxidation

    R Universal gas constant

    T Absolute temperature

    Z Thickness of the oxide scale

    C ConstantKp Scaling constant

    o Density of the oxide

    F Particle flux rate

    L Depth to which the deformed zone extends

    W Indentation diameter

    Constant

    H Hardness

    U Crater volume

    mp Mass of single erodentr Radius of the erodent

    N Number of erodents

    Semi included angle of conical erodent

    tb Time between impacts

    tim Time of impact

    Zb Thickness of the oxide scale grown between two

    successive impacts

    1. Introduction

    Erosive wear or solid particle erosion is sometimes known

    as impact wear. Solid particle erosion is defined as material

    degradation due to the impact of particles travelling withsome significant velocity. It is mechanistically different from

    other forms of erosion such as liquid impact erosion, slurry

    0022-3727/06/060101+24$30.00 2006 IOP Publishing Ltd Printed in the UK R101

    http://stacks.iop.org/JPhysD/39/R101http://stacks.iop.org/JPhysD/39/R101http://dx.doi.org/10.1088/0022-3727/39/6/R01
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    Topical Review

    Table 1. Examples of systems subjected to elevated temperature erosion.

    System Components References

    Combustion systems Burner nozzles, reheater, super heater, [5,6]economizer tube banks, boiler heat exchanger,in bed tubes, tube banks, etc

    Coal gasification systems Turbine, lock Hopper valves [7]Coal liquefaction system Valve to throttle the flow of product stream [7]Gas turbines Blades [8]

    erosion and cavitation erosion, etc. A tribosystem suffering

    from erosive wear can be characterized as an open system.

    In such a system, the counterbody is continuously replaced.

    Another important feature of solid particle erosion is that

    the wear of the counterbody is completely uninteresting. In

    solid particle erosion, the contact time between the erodent

    and the target material is only momentary. In this respect,

    erosion is different from other related processes such as sliding

    wear, abrasive wear, grinding and machining, etc, in which thecontact between the tool/abrasive and the target/work piece is

    continuous.

    Room temperature erosion is an important problem

    in several engineering applications. Rocket motor trail

    nozzles [1], the engine of a helicopter operating in dusty

    terrain [2], equipment in oil and mining industries [3, 4],

    etc are subjected to solid particle erosion at ambient

    temperature. Several engineering components are degraded

    dueto solid particle erosion at elevated temperature. A number

    of industrial systems, which undergo erosion at elevated

    temperature, are summarized in table 1 [58]. At the same

    time, it should be mentioned that erosion could also be used

    constructively, as in the case of shot peening, sand blasting,mining, rock drilling and cutting applications, etc [911].

    Erosion behaviour of metallic materials at room

    and elevated temperatures has been reviewed in several

    publications [1220]. The information contained in these

    reviews will be repeated only to the extent of impressing upon

    the readers the essential features of the erosion processes. It

    is not the purpose of this work to provide a comprehensive

    review of the status of research in the field of solid particle

    erosion at elevated temperature; rather the aim is to discuss

    and review some of the recent results which have enhanced

    our understanding in the areas of elevated temperature erosion

    of metallic materials. This review will be confined only to

    metals and alloys. Elevated temperature erosion of ceramics,glasses and composites will not be considered here.

    For the purpose of convenience, the review is divided into

    several sections. Section 2 consists of elevated temperature

    erosion tests. The salient features of elevated temperature

    erosion constitute section 3. Examination of the eroded

    surfaces is consideredin section 4. Section 5 dealswitherosion

    oxidation interaction. Erosion enhanced oxidation kinetics

    is analysed in section 6. Future research areas for elevated

    temperature erosion arediscussed in section 7. Thisis followed

    by concluding remarks in section 8.

    2. Elevated temperature erosion test

    Over the last few decades several test techniques or

    methodologies have been developed for studying mechanisms

    and assessing the extent of erosion. These tests can broadly

    be divided into two categories, namely (1) those simulative

    tests that are designed to simulate a specific type of erosion

    and (2) those that are intended to be used for fundamental

    studies. The main problem of the simulative test is that it is

    very expensiveandit is difficult toconduct fundamental studies

    for material development or for understanding the mechanisms

    of erosion. In order to avoidtheseproblems, various laboratory

    tests have been developed.The most common laboratory test involves blasting a

    stream of airborne particles against the target as standardized

    by G 76-83 [21]. In this type of test, a known quantity

    of erodent is fed into an air stream, accelerated through a

    converging nozzle and directed towards the test specimen. A

    cleaned andweighed sampleis exposed to theparticle-laden air

    streamfora predetermined time andweighed after interrupting

    the test. The ratio of the weight loss suffered by the sample to

    the weight of erodent gives the dimensionless erosion rate.

    The air jet-type elevated temperature erosion rigs can be

    classified into two broad groups. The first group comprises

    erosion rigs, which are designed in such a fashion that both

    the fluid stream carrying the particles and the eroding target

    are heated to the same test temperature. These are called

    isothermal erosion rigs. On the other hand, the second group

    of erosion rigs, called non-isothermal rigs, have the facility to

    heat the target material alone, while the fluid stream with the

    particles is not preheated before allowing it to enter the erosion

    chamber. In these types of rigs, the colder fluid stream cools

    the target materials to some extent on impact. Nevertheless,

    the target material still attains a steady-state temperature. The

    above classification of the erosion rig as isothermal and non-

    isothermal is largely artificial for reasons stated below.

    1. The test specimen attains a constant temperature and

    remains at that temperature throughout the test in both

    types of rigs.2. The erodents are not heated and the cold particles impinge

    thetarget material. However, unlikein thecase ofabrasion

    or sliding wear, the contact between the particles and the

    target materials in the case of solid particle erosion is

    momentary, and hence negligible transfer of heat takes

    place between the particles and the substrate. Thus, it is

    immaterial as to whether theparticlesarepreheatedor not.

    The non-isothermal erosion rigs are easy to fabricate but

    they fail to simulate the erosion conditions. Hence, such rigs

    are not popular at present. In contrast, isothermal type erosion

    rigs can simulate erosion conditions but they are difficult to

    fabricate. The schematic diagram of one such erosion rig,

    fabricated by the author at DMRL, is shown in figure 1. Theunique feature of this rig is its ability to alter the particle

    feed rate by over 100 times. Its particle feeding system is

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    Air Heating

    System

    Temperature

    Controller

    For Air Heating

    System

    Air Pressure Indicator

    Air Flow Rate IndicatorFluidized

    Chamber

    Test

    Chamber

    Sample

    HoldingDevices

    Particle Feeding System

    Temperature

    Indicator of

    Hot Air

    Temperature

    Indicator of

    The Sample

    Outlet

    Inlet

    Air Heating

    System

    Temperature

    Controller

    For Air Heating

    System

    Air Pressure Indicator

    Air Flow Rate IndicatorFluidized

    Chamber

    Test

    Chamber

    Sample

    HoldingDevices

    Particle Feeding System

    Temperature

    Indicator of

    Hot Air

    Temperature

    Indicator of

    The Sample

    Outlet

    Inlet

    Temperature

    Controller of the

    Test Chamber

    Figure 1. Schematic representation of jet type elevated temperature erosion rig [67].

    a miniaturized conveyer belt system and particle feed rate is

    controlled by controlling the speed of the motor of the system.

    Further description of this rig is available elsewhere [22].

    The test procedure involves heating the compressed air

    to the required temperature and then heating and soakingthe test sample to that temperature. The heated samples are

    then exposed to compressed, heated, fluidized and accelerated

    air streams carrying the particles. The elevated temperature

    erosion test is a multiple specimen test procedure. Cleaned,

    dried and weighed samples are exposed to erodents for various

    time intervals (say t1, t2, t3, . . . , where t1 < t2 < t3)

    corresponding to various mass of erodents (m1, m2, . . . , mn).

    A similar number of samples are again exposed to an air stream

    without carrying particles. IfM1, M2, . . . , M n represent the

    mass loss suffered by n samples when exposed to erodents for

    time intervals oft1, t2, . . . , t n and ifM

    1, M

    2, . . . , M

    n are the

    massgainsexperienced by n samples when exposed to theplain

    air stream without erodents for time intervals of(t1, t2, . . . , t n)then the incremental erosion rate E1, E2, . . . , En can be

    computed as

    En =(Mn M

    n) (Mn1 M

    n1)

    mn mn1. (1)

    This procedure is repeated until En1 is equal to En2 and

    this E is considered to be the incremental erosion rate.

    The main problem of the jet type of erosion rig is the

    measurement of impact velocity. There are three different

    types of velocity measurement techniques available. In the

    first method, known as the photographic method, a high-

    speed camera is used to photograph the successive positionsof a single particle as a function of time and thus compute

    the velocity. The second method, known as the rotating

    disc method, was developed by Ruff and Ives [23]. In this

    method velocity is determined by estimating the time of flight

    of particles between two discs fixed on a common shaft

    rotating at some specified velocity. A modified version of

    the rotating disc is the paddle wheel technique [24]. Thismethod gives a more reliable and statistically more accurate

    velocity.

    The third method uses the laser Doppler velocitimeter

    (LDV). This technique is an accurate, non-interactive and

    on-line velocity measuring device. The LDV uses the well-

    known Doppler effect to measure the velocity of the particles.

    When light is scattered from a moving object, the stationary

    observer will see a change in the frequency of scattered light

    proportional to the velocity of the object. A laser is used as a

    light source because it is easily focused and is coherent.

    In many applications, for example, pipe bends in a slurry

    transportation system, the impact is primarily by big particles

    with very low impact velocity. To simulate such a system,samples are impacted by dropping particles under gravity.

    Such a system was first introduced by Bitter [25], a schematic

    presentationof which is shown in figure 2. The system consists

    of a ball dispenser unit, the velocity measuring system, ball

    counting unit and the sample holder. The ball dispenser and

    the sample holder can be moved up and down so as to alter the

    height over which the eroding particle falls. Before the steel

    ball impacts thesampleit passesthrough a multiple photodiode

    unit, which measures the velocity of the passing ball and,

    in addition, keeps track of the total number of balls passing

    through.

    Whirling arm rigs were developed to enable tests to be

    carried out at precisely controlled velocity over a range ofimpact conditions. The target specimens are attached to the

    tips of the rotor arms and whirled through a certain or a

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    Ball

    Feeder

    Timer

    Sample

    Holder

    Velocity MeasuringSystem

    Figure 2. Schematic diagram of low velocity erosion rig.

    Figure 3. Schematic diagram of whirling arm erosion rig.

    narrow band of erosive particles. These rigs are very noisy

    and consume considerable power. A whirling arm erosion

    rig is schematically shown in figure 3. These kinds of rigs

    simulate the degradation conditions prevalent in the fluidized

    bed combustor. The whirling arm erosion rig was initially

    developed by Tilly and Sage [26]. One of the advantages of

    this type of rig is that the erodent velocity can be controlled

    precisely as the velocity is governed by the rotating speed of

    the arms. It also permits testing to be carried out over a widerange of impact velocities. It makes efficientuse of theerodent

    as theentire amountof erodent is delivered to thetarget sample.

    3. Salient features of elevated temperature erosionof metallic material

    Over the last decade or so, a substantial amount of work on

    elevated temperature erosion of metals and alloys has been

    carried out [2762]. A compilation of these investigations,providingdetails of materialssubjectedto elevatedtemperature

    erosion and the test conditions, is made in table 2. These

    tests cover a wide range of test conditions and test materials.

    Based on the work of the investigators compiled in table 2, the

    important factors which influence the solid particle erosion

    behaviour of metallic materials at elevated temperature are

    described below.

    3.1. Effect of temperature

    The variation of erosion rate with temperature for a number

    of metals and alloys is depicted in figures 4 and 5 [27, 28].

    The erosion data presented in these figures pertain to highimpact velocities and mostly with angular particles. The

    observed temperature dependence of the erosion rate can be

    classified into three groups. In the first group, the erosion

    rate initially decreases with the increase of temperature,

    reaches a minimum and then starts increasing with increasing

    temperature. Materials such as 5.0Cr0.5Mo, 17-4 PHSS,

    410 SS, Alloy 800, Ti-6Al-4V, and tungsten belong to this

    group. The second group comprises metals such as Ta and

    lead (for oblique impact) andalloyssuch as 310SS (for oblique

    impact), 1018 steel and 1100 aluminium (for normal impact)

    which exhibit a temperature independent erosion rate up to a

    critical temperature followed by an increase of the erosion rate

    with increasing temperature. Finally, group three materialsshow a monotonically increasing erosion rate with increasing

    temperature. Inco 600, carbon steel, 12Cr1MoV steel, and

    2.25Cr1.0Mo steel, lead and 20245 Al are some of the typical

    examples in this group.

    3.2. Effect of impact velocity

    The velocity dependence of erosion rate (E) is characterized

    by the velocity exponent, p, given by

    E = K1Vp, (2)

    where K1 is a constant and V is the impact velocity. The

    velocity exponents (p) obtained by various investigatorsare plotted in the velocitytemperature regime in figure 6.

    The velocity exponent decreases with an increase in erosion

    test temperature for 304 SS to values as low as 0.9 at low

    impact velocities. At relatively higher impact velocities p

    appears to lie in the range 23. Levy and Man [29, 30]

    reported the influence of erodent size on the velocity exponent

    for erosion of 9Cr1Mo steel at 923K using angular SiC

    particles.

    3.3. Effect of impact angle

    The available data related to erosion rate and impact angle at

    different temperatures are presented in this section. However,most of the metallic materials, irrespective of temperature of

    erosion, exhibit a ductile behaviour, i.e. a maximum erosion

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    Table 2. Compilation of the work of various investigators on elevated temperature erosion of metallic material.

    Materials Name of the investigators Test conditions

    310 SS, 304 SS, 1018, 2.25Cr1.0Mo, Levy et al [27] Nitrogen gas, 240 m SiC, V = 30ms1,5.0Cr0.5Mo, 410 SS, 17-4 PHSS T = RT to 1173K, = 30 and 90

    1100 Al, 310 SS Finnie et al [32] Nitrogen gas, 250 m SiC, V = 3060 m s1,

    T = RT to 0.8 Tm, = 30

    9Cr1.0Mo, 2.25Cr1.0Mo, 5.0Cr10.5Mo, Levy and Man [29, 30, 47] Air, 130 m SiC and SiO2, V = 35ms1,

    304 SS, 410 SS T = 9231123K, = 90 and 30

    410 SS Levy et al [45] Air, 5 m fly ash, 130 m Al2O3,T = 1223K, V = 5 m s1, = 45

    5.0Cr0.5MoSi Levy and Wang [40,48] Air, 90 m alumina, V = 30, 40 and 70m s1,T = 1123K, = 9

    Inco 600 Tabakoff and Vittal [34] Air, 100800 m quartz, V = 60250ms1,T = 544, 666 and 846K, = 1070

    Ti6Al-4V, 2074 Al, 410 SS, W, Ta, Pb Gat and Tabakoff [28] Air, 86 m quartz, V = 180300m s1,and 304 SS T = 3001023K, = 1590 also 164 m quartz,

    V = 120ms1, T = 300483K, = 20, 60 and 90

    Ni, Co Kang et al [50] Nitrogen, air, 20 m alumina, V = 90 and 140m s1,T = 9231073K, = 90

    Ni, Co Chang et al [38, 47] Air, 20 m alumina, V = 140, 123 and 70m s1,

    T = 8731053K, = 90

    , 60

    , 30

    and 20

    AISI 303 Shayler and Yee [31] Air, 4766 m fly ash, V = 150300 m s1,T = 300773K, = 35

    304 SS, alloy 800, C-steel, 2.25Cr1.0Mo, Shida and Fujikawa [42] Argon gas, 120 m quartz, V = 40120m s1,12.0Cr1.0MoV T = 673923K, = 2090

    304 SS, 316 SS and 410 SS Singh and Sundararajan [43] Air, 160 m SiC, V = 55110ms1,T = 300773K, = 30, 60 and 90

    In 738, X 40, MA 754 and HA 188 Barklow et al [51] Burner rig, 20 m alumina, V = 200275 m s1,T = 1148 K

    Stellite 6B and 1, In-100, MA-754, HA 8077, Wright et al [52] Argon gas, air, 12 m alumina, V = 43ms1,AISI 446 SS, FeCrAlY, AISI 446 T = 1033K, = 30

    9.0Cr1.0Mo, 304 SS Sethi and Wright [53] Air, 1 m alumina, V = 2.7 and 4.3 m s1,T = 7331100K, = 30

    304 SS, 416 SS, 430 SS and 17-4 PH SS Zhou and Bahadur [35] Air, 120 grit SiC, V = 65ms1,T = 9231073K, = 30

    2.25Cr1.0Mo Sethi and Carey [54] Air, 1 m alumina, V = 2.7 m s1,T = 763863K, = 30

    Alloy 800 HT, 310 SS Stott et al [55] Air, 4766 m fly ash, V = 150300 m s1,T = 300773K, = 35

    Haynes 188, Waspaloy Chinadurai and Bahadur [56] Air, 150 m SiC, V = 50ms1,T = 3001073K, = 30

    Ti6Al-4V Zhou and Bahadur [57] Air, 4766 m fly ash, V = 50ms1,T = 3001073K, = 1090

    Carbon steel Xie and Walsh [58] Air, 43 m coal ash, V = 530ms1,T = 423673K

    FeCrC cast steel Drotlew et al [59] V = 65ms1, T = 723K, = 1560

    Ni, Ni20Cr Manish Roy et al [60] Air, 200 m SiO2, V = 35, 65 and 105m s1,

    T = 3001073K, = 30, 45, 60 and 90

    Fe3Al base alloy, Ni, Co Yu et al [61] SO2, air, 2050 m SiO2, V = 160190 m s1,

    T = 8731073K, = 090

    FeCrC Hayashi et al [62] Air, 23 m cold silica, V = 80ms1, T = 973K

    Note: T = test temperature, V = impact velocity and = impact angle.

    rate at oblique impact angles (1030). The universality

    of such an observation is shown in figures 7 and 8,

    wherein data from a large number of investigators have been

    compiled [3136].

    Levy [37] obtained a higher erosion rate at normal impact

    than at oblique impact for 9Cr1Mo steel at 1123K using

    rounded Al2O3 (130 m) erodent for a range of impact

    velocities (3070 m s1), as shown in figure 9. But at a low

    impact velocity of 20 m s1, a maximum in the erosion rate

    occurred at oblique impact angle. Observations by Chang et al

    [33, 38] shown in figure 10 indicate that the peak erosion rateof Co at a test temperature of 1053K occurs at an impact angle

    of 60 when impacted with 20 m angular alumina particles at

    impactvelocities of 70140m s1. However, when the erosion

    test is carried out at 873 K and at impact velocity of 140m s1,

    the erosion rate peaks at an impact angle of 30. Thus, there

    exist apparently conflicting observations regarding the erosion

    rateimpact angle behaviour.

    3.4. Effect of particle size

    Tabakoff and Vittal [34] carried out erosion tests on Inco 600

    alloy using quartz particles having sizes between 70 and

    800 m. Their work indicates that the erosion rate increasesmarginally with the increase of particle size, as shown in

    figure 11. Zhou and Bahadur [35] investigated the effect

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    of the particle size of SiC on the erosion rate of 304 SS

    at 923 K (impact angle: 30 and impact velocity: 65 m s1).

    These results indicate that erosion rate increases with the

    increase in particle size up to 40 m and thereafter it becomes

    independent of the particle size (figure 12). Levy et al

    [29, 30, 37, 39], however, noted only the increase of erosion

    rate with the increase of particle size for 9Cr1Mo steel eroded

    at a temperature of 923K and that for 1018 steel eroded

    at 723 K.

    0

    20

    40

    60

    80

    100

    120

    0 200 400 600 800 1,000 1,200

    Temperature (K)

    ErosionRatex

    106(

    Kg/Kg)

    310 SS

    304 SS

    410 SS

    2.25Cr-0.5Mo

    17-4 PHSS

    1018 Steel

    5.0Cr-0.5Mo

    Impact Velocity : 30 m/s

    Impact Angle : 30o

    Erodent : SiC (250 m)Gas : Nitrogen

    Figure 4. Variation of erosion rate with temperature for a number ofalloys [27].

    20

    30

    40

    50

    60

    70

    80

    90

    100

    110

    120

    283 303 323 343 363 383 403 423

    Temperature (K)

    ErosionRatex104(

    Kg/Kg)

    Lead

    Impact Angle : 20o

    Impact velocity : 120 m/s

    Erodent : Quartz ( 138 - 164 m)

    0

    20

    40

    60

    80

    100

    120

    140

    283 303 323 343 363 383 403 423

    Temperature (K)

    ErosionRatex104(

    Kg/Kg)

    Impact Angle : 90o

    Impact velocity : 120 m/s

    Erodent : Quartz ( 130 m)

    Lead

    Tungsten

    0

    1

    2

    3

    4

    5

    6

    7

    8

    9

    10

    283 333 383 433 483

    Temperature (K)

    Erosionratex104

    (Kg/Kg)

    2024 Al

    Ta

    Ti-6Al-4V

    410 SS

    Impact Angle : 20o

    Impact velocity : 120 m/s

    Erodent : Quartz ( 138 - 164 m)2

    2

    3

    3

    4

    4

    5

    283 333 383 433 483

    Temperature (K)

    ErosionRatex104(

    Kg/Kg) Ta

    2024 Al

    410 SS

    Ti-Al-4V

    Impact Angle : 90o

    Impact velocity : 120 m/s

    Erodent : Quartz ( 138 - 164 m)

    Figure 5. Effect of test temperature on the erosion rate of a number of metals and alloys [28].

    3.5. Effect of particle shape

    Levy et al [29, 30, 37, 39, 40] investigated the erosion rate of

    a number of Cr containing steels at 1123 K with angular SiC

    and spherical Al2O3 as erodent particles. A typical result for

    9Cr1Mo steel is presented in figure 13. The erosion rate is

    significantly higher when SiC is used as the erodent.

    3.6. Effect of particle feed rate

    Zhou and Bahadur [41] have investigated the influence of the

    particle feed rate on the erosion rate of 304 and 430 SS over

    a large temperature range. The reported results as illustrated

    in figure 14 suggest that up to a temperature of about 773 K

    increasing the feed rate by a factor of 16 has no influence on

    the erosion rate. However, beyond 773 K, a lower feed rate

    results in a substantially higher erosion rate. Roy et al [60]

    also noted a decrease of erosion rate with the increase of the

    particle feed rate, especially at low impact velocity.

    3.7. Effect of eroded material characteristics

    The interpretation of the available data on the effect of eroded

    material characteristics on its erosion rate is complicated by

    the fact that the behaviour of the oxide scale under erosion

    conditions needs to be considered in addition to the behaviour

    of the metallic material per se. The oxidation characteristic

    of the eroded material plays a more important role than the

    mechanical properties of the eroded materials at elevated

    temperature.

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    P values given alongside data points

    Figure 6. Velocity exponent obtained by various investigators,plotted in velocitytemperature regime.

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    0 10 20 30 40 50 60 70 80

    Impact Angle (Degrees)

    ErosionRatex104

    (Kg/K

    g)

    850 K

    644 K

    766 K

    Material : INCO 600

    Impact Velocity : 183 m/s

    0

    1

    2

    3

    4

    5

    6

    10 20 30 40 50 60 70 80 90

    Impact Angle (Degrees)

    ErosionRatex104(

    Kg/Kg)

    Material : 303 SS

    Impact Velocity : 130 m/s

    291 K

    1023 K

    0.000

    0.005

    0.010

    0.015

    0.020

    0.025

    0.030

    0.035

    0.040

    0.045

    0.050

    0 20 40 60 80 100

    Impact Angle (Degrees)

    MaximumThicknessLoss(m/s)

    Test Temperature = 573K

    Impact Velocity = 120 m/sErodent = quartz (120 m)

    304 SS

    Cr-Mo-V

    C Steel

    0

    1

    2

    3

    4

    5

    6

    0 20 40 60 80 100

    Impact Angle (Degrees)

    ErosionRatex104(

    Kg/Kg)

    1255 K

    293 K

    293K

    1093 K

    558 K372 K

    743 K

    Impact Velocity = 61 m/sImpact Velocity = 31 m/s

    Erodent = SiC (250 m)Fluidizing Gas = Nitrogen

    Al

    310 SS

    ab

    cd

    Figure 7. Variation of erosion rate with impact angle at various test temperatures: (a) INCO 600 [34], (b) 303 SS [31], (c) CrMoV, carbonand 304 SS [42] and (d) aluminium and 310 SS [32].

    Even at elevated temperature, if one considers the erosion

    behaviour of metallic material at high impact velocities and

    feed rates, the oxidation plays an insignificant role and the

    erosion behaviour is essentially metal erosion behaviour. The

    experimental data of Shida and Fujikawa [42] pertaining to

    1.25 Cr1MoV, 2.25CrMo, 12Cr1MoV and plain carbonsteel (up to 923 K), that of Singh and Sundararajan [36, 43]

    pertainingto 304, 316, 410 stainless steel (up to773 K)and that

    of Levy et al [44, 45] pertaining to 2.25Cr1.0Mo steel, 5Cr

    0.5Mo steel, 1018steel, 304 SS, 310 SS, 410 SSand17-4PHSS

    can be considered elevated temperature erosion of metals with

    minimum or negligible oxidation. Under such conditions the

    dependence of the strength of the material on temperature is a

    reasonable indicator of the temperature dependence of erosion

    resistance of the materials. Erosion data further indicate that

    austenitic stainless steels have superior resistance to elevated

    temperature erosion than ferritic steels. The 410 stainless

    steel having a tempered martensitic matrix exhibits an erosion

    resistance comparable to that of austenitic stainless steels.The oxidation effect is reported to be important for

    elevated temperature erosion tests conducted at low impact

    velocities and using rounded Al2O3 as an erodent. The

    influence of Cr content on the erosion rate of steel is

    illustrated in figure 15. It is indicated that the erosion rate

    decreases to a very low value when Cr content in the steel

    exceeds 1012% [35]. In the case of steel having Cr less than

    10%, thick Fe2O3 scale was formed during erosion leading to

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    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    10 20 30 40 50 60 70 80 90

    Impact Angle (Degrees)

    ErosionRatex104 (Kg/Kg)

    Material : 304 SS

    Impact Velocity : 305 m/s

    1173 K

    873 K

    0

    2

    4

    68

    10

    12

    14

    16

    10 20 30 40 50 60 70 80 90

    Impact Angle (Degrees)

    ErosionRate

    x104(

    Kg/Kg) Material : 304 SS

    Impact Velocity : 183 m/s1173 K

    873 K

    0

    1

    1

    2

    2

    3

    3

    0 20 40 60 80 100

    Impact Angle (Degrees)

    ErosionRatex104(

    Kg/Kg)

    773 K

    297 K

    Material : 304 SS

    Impact Velocity : 70 m/s

    4

    5

    6

    7

    8

    9

    10

    11

    12

    13

    14

    20 30 40 50 60 70 80 90 100

    Impact Angle (Degrees)

    ErosionRatex104(

    Kg/Kg)

    316 SS

    410 SS

    Impact Velocity : 129 m/s

    763 K

    RT

    548 K

    a b

    c

    d

    Figure 8. Influence of impact angle and test temperature on erosion rate of (a) 304SS, (b) 304SS, (c) 304SS [35] and (d) 410SS and316SS [43].

    high erosion rates [46]. Theexperimental results of Chang etal

    [47], presented in figure 16, also indicate the importance of

    the nature of the scale that forms during erosion at elevatedtemperature. It is also noted that materials with high scaling

    rate such as nickel and cobalt exhibit the highest erosion

    rates, while the alumina-forming alloys such as CoCrAlY and

    NiCrAlY exhibit intermediate erosion rates. The superiority

    of the Al2O3 forming alloy stems from the fact that the Al2O3forming scale forms much more slowly than the Cr2O3 scale.

    Extensive work by Levy andco-workers [37,39,44,48,49]

    implies that the morphology of the oxide scale that forms

    during erosion is important. Segmented scales have a better

    erosion resistance than thick, continuous and dense scale since

    the spalled area is confined to oxide crystalline only in the case

    of erosion of the segmented scale. A striking illustration of the

    abovefact is obtained when Si is added to steels. Addition of Sito low chromium steel results in the formation of a segmented

    scale even at high impact velocity and thereby reduces the

    erosion rate substantially as compared with the same steel

    without Si [49].

    The above discussion clearly brings out certain features

    of elevated temperature erosion of metallic materials. Almost

    all metallic materials exhibit ductile erosion response at room

    temperature, whereas at elevated temperature both brittle and

    ductile erosion responses are noted [31, 36, 37]. The velocity

    exponents for metallic materials are 2.5 during ambient

    temperature erosion. At elevated temperature the velocity

    exponent of metals and alloys varies over a wide range from

    0.9 to even more than 3.0 [3133]. It is established that theerosion rate at room temperature increases with the increase

    of the particle size up to 50 m and beyond such magnitude

    0

    5

    10

    15

    20

    25

    30

    35

    40

    45

    0 20 40 60 8 00

    Impact Angle (Degrees)

    MetalThicknessLoss(m) 70 m/s

    45 m/s

    35 m/s

    25 m/s

    Figure 9. Variation of metal thickness loss with the impact angle for

    9.0Cr1.0Mo steel at 1123 K [37].

    the particle size has no effect on the erosion rate. Reported

    literature indicates that the erosion rate increases with the

    increase of particle size at high temperature [29,30,34,39]. At

    ambient temperature, changing theparticle shape from angular

    to spherical results in altering the erosion response from brittle

    to ductile [63, 64]. At elevated temperature, brittle to ductile

    response is noted irrespective of the particle shape [29,30,37].

    Particle feed rate has a negligible effect on room temperature

    erosion rate [6567]. A remarkable effect of the particle

    feed rate has been noticed at elevated temperature [29]. The

    characteristics of mechanical properties of eroding material

    particles have nominal influence on room temperature erosionbehaviour [56, 6875]. In contrast, this aspect at elevated

    temperature is hardly explored.

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    0.0

    0.5

    1.0

    1.5

    2.0

    2.5

    3.0

    0 20 40 60 8 00

    Impact Angle (Degrees)

    ErosionRate(x10

    -1,Kg/m2sec) 1053 K, 140 m/s

    873 K, 140 m/s

    873 K, 70 m/s

    Figure 10. Variation of erosion rate of Co with the impact angle at1053 K [38].

    0

    1

    2

    3

    4

    5

    6

    7

    0 100 200 300 400 500 600 700 800 900

    Particle Size (m)

    ErosionRate(m3/Kg)x10

    Figure 11. Influence of particle size on the erosion rate of Inco 600alloy [34].

    0

    50

    100

    150

    200

    250

    300

    350

    400

    0 20 40 60 80 100 120 140 160

    Particle Size (m)

    ErosionRate(Kg/Kg)

    Figure 12. Effect of particle size on the erosion rate of 304 SS at923 K [35].

    4. Examination of eroded surfaces

    At elevated temperature, the material removal is governed

    by the synergistic effect of erosion and oxidation (EO).

    Detailed examination of the eroded target material using a

    scanning electron microscope (SEM), a transmission electronmicroscope (TEM) and an optical microscope (OM) has been

    carried out. The advent of single particle experiment is

    0

    50

    100

    150

    200

    250

    300

    0 10 20 30 40 50 60 7 0

    Impact Velocity (m/s)

    WeightLossx10-6 (Kg/Kg)

    9Cr 1 Mo Steel

    Nozzle Tester Corrosion Erosion Air

    Particle Size: 130 m

    Test Temperature : 1123K

    Test Time: 2 hr

    SiC

    Al2O3

    30o

    30o

    90o

    90o

    Figure 13. Variation of weight loss with impact velocity for9.0 Cr1.0Mo steel at 1123K showing the effect of particle feedrate on erosion behaviour [37].

    0

    50

    100

    150

    200

    250

    300

    350

    400

    450

    0 200 400 600 800 1,00 ,200

    Test Temperature (K)

    ErosiveMassLossRate(Kg/Kg) Erodent Concentration

    2.6x10-6

    Kg/m2s

    42.0x10-6

    Kg/m2.s

    Material:

    304 SS

    430 SS

    Figure 14. Variation of erosion rate of 304 SS and 430SS with testtemperature showing the effect of feed rate on erosion rate [41].

    particularly fruitful since such experiments allow a detailed

    examination of large, individual craters. On the basis of

    the extensive literature [57, 67, 7678], four different types of

    EO mechanisms can be envisaged: in the first case, at low

    temperatures, at high impact velocities and feed rates, there is

    no oxide scale. Even if there is any oxide scale, it will be very

    thin and it will be able to deform in the same manner as that

    of the substrate target. Under such circumstances, erosion

    takes place from the metallic surface and this mechanism

    of erosion is called metal erosion. The erosion behaviourin this regime is similar to the ambient temperature erosion

    behaviour of metallic materials. The erosion response in the

    metal erosion regime is ductile, the velocity exponent of the

    erosion behaviour is between 2 and 3 and the erosion rate

    is independent of the particle feed rate. The metal erosion

    mechanism is schematically shown in figure 17(a). In the

    metal erosion regime, there are two modes by which materials

    can be removed. These modes are ploughing and cutting. In

    general, when a particle is in contact with a target at positive

    rake angle, the cutting mode operates. On the other hand, the

    ploughing mechanism operates at negativerake angle. Cutting

    mechanisms result in generation of new surfaces while the

    ploughing mechanism involvesthe displacement and extrusionof the material with no new surface generation. In addition,

    the cutting mode is more efficient than the ploughing mode

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    0

    20

    40

    60

    80

    100

    120

    0 5 10 15 20 25 30

    Chromium Content (wt %)

    MetalThicknessLoss

    (m)

    Normal Impact

    Oblique Impact

    Test Temperature : 1123 K

    Impact velocity : 35 m/sErodent: Al2O3, 130 mFluidizing Medium: Air

    310 SS304 SS

    410SS

    9Cr

    5Cr

    2.25Cr

    Figure 15. Influence of Cr content on the erosion rate of steel [35].

    when considered in terms of energy consumed per unit volume

    removal of the target material. The work carried out by a large

    number of investigators [7982] has revealed that almost all

    metals and alloys lose material by the formation of a lip and

    its subsequent fracture.

    Inmetalsand alloys, duringerosion,once thelip is formed,

    it is fractured by several modes. In the case of ductile metals

    like copper [83], brass [83], aluminium [84] and iron [85]

    the lip fracture occurs by necking, and the resulting fracture

    is ductile, as exemplified by the dimpled fracture surface.

    This mode of lip fracture is shown in figure 18(a). In the

    case of a high strength alloy such as CuBe in age hardenedcondition [83], 301 SS [85] and TD nickel [85] the lip removal

    is greatly aided by the formation of adiabatic shear bands at

    the base of the lip as shown in figure 18(b) and subsequent

    easy separation/fracture across this band. In this case also

    the fracture is ductile, as indicated by the presence of shear

    dimples on the fracture surface. These two modes of material

    removal considered above involve the fracture of pre-existing

    lips. On the other hand, a new mode termed adiabatic

    shear induced spalling involves the formation of intersecting

    adiabatic shear bands at the base of the crater and subsequent

    removal of chunks of material as illustrated in figure 18(c).

    This mode of weight loss, which is highly efficient in terms of

    energyexpendedper unit volumeof targetmaterial removed, isimportant only at normal impact where maximum resistance

    is offered to curtail spreading of deformation. The erosion

    response under such circumstances will be similar to that

    observedforceramic materials. But theunderlyingmechanism

    is entirely different. In the case of ceramic materials, material

    removal occurs with the formation of intersecting cone or

    radial cracks, which nucleate from pre-existing flaws once a

    critical tensile stress is exceeded. Further, these cracks are

    essentially brittle in nature. On the other hand, formation of

    anadiabaticshearbandrequires critical strain[86]. In addition,

    the fracture surface resulting from adiabatic shear induced

    spalling exhibits sheardimples, implying an essentiallyductile

    fracture.On the other extreme, at very high temperatures and low

    velocities and particle feed rates, erosion takes place from

    the oxide scale only, as shown in figure 17(b). Under such

    conditions, a thick oxide scale is formed on the target material

    during erosion and the deformed zone formed due to impact is

    confined within the oxide scale. The erosion behaviour from

    the oxide scale is characterized by a brittle erosion response,

    strong velocity dependence and particle feed rate independentof the erosion rate. This erosion mechanism is termed oxide

    erosion. In oxide erosion, material removal occurs with

    the formation of intersecting cones and radial cracks, which

    nucleate from pre-existing flaws once a critical tensile stress

    is exceeded. At an intermediate temperature, impact velocity

    and particle feed rate, an oxide scale of intermediate thickness

    is formed. However, the depth of the deformed zone extends to

    the metallic substrate beyond the oxide scale. Consequently,

    the oxide scale beneath the eroding particle tends to crack, gets

    pushed down into much softer base material and in the process

    the softer base material gets squeezed out onto the top surface

    through the cracks in the oxide scale. Over a period of time,

    the repetition of such a process during each impact causes the

    formation of a composite layer comprising the bulk metal and

    broken pieces of oxide scale. Erosion takes place from this

    composite layer. This mechanism, presented schematically

    in figure 17(c), is termed oxidation affected erosion. The

    interesting aspect of oxidation affected erosion is that the

    volumefractionof theoxidein thecomposite layer isa function

    of erosion conditions such as temperature, impact velocity

    and particle feed rate. As a result, the erosion behaviour

    in the oxidation affected erosion regime can vary from a

    ductile to a brittle response depending on the amount of oxide

    scale present in the composite layer. Further, unlike in the

    case of metal erosion or oxide erosion, the oxidation affectederosion rate depends strongly on the test temperature and

    particle feed rate. The final erosion mechanism is oxidation

    controlled erosion and this is illustrated in figure 17(d). At

    relatively higher temperaturesandlowerparticle feed rates and

    impact velocities, the oxide scale that forms during erosion

    is brittle and non-adherent. In such cases, the oxide scale

    gets removed after it attains a critical thickness. The erosion

    behaviour in this regime exhibits a brittle erosion response,

    weak velocity dependence and particle feed rate dependent

    erosion rate. Figures 19 and 20 show SEM images of the

    morphologies of the eroded surfaces and transverse sections

    of the eroded surfaces, obtained after exposing commercially

    pure Ni to elevated temperature erosion. All the four

    mechanisms described schematically in figure 17 can be seen

    under SEM.

    5. Erosion oxidation interaction

    As mentioned previously, the erosion behaviour of metallic

    materials at elevated temperature is governed by the nature

    of interaction between erosion and oxidation. The nature of

    interaction between erosion and oxidation in turn depends on

    the thickness, morphology, adherence and the toughness of

    the oxide scales that form in these materials. Before goinginto the details of mechanisms it is important to deal with the

    theoretical aspects.

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    0.0

    0.5

    1.0

    1.5

    2.0

    2.5

    3.0

    3.5

    4.0

    1 2 3 4 5 6

    ErosionRate(Kg/m2s)x106

    Co

    MA-754Ni-30Cr

    CoCrAlY

    Ni-20Al

    Test Temperature : 1053 K

    Impact Velocity : 140 m/s

    Impact Angle : 30o

    Erodent : Al2O3 (20 m)

    0.0

    0.5

    1.0

    1.5

    2.0

    2.5

    0

    1 2 3 4 5 6

    ErosionRate(Kg/m2s)x106

    Ni

    Co

    MA-754 Ni-30Cr

    CoCrAlY

    Ni-20Al

    Test Temperature : 873 K

    Impact Velocity : 140 m/s

    Impact Angle : 30o

    Erodent : Al2O3 (20 m)

    Ni

    (a)

    3.(b)

    Figure 16. Bar diagram showing the erosion rates of various alloys forming different types of scale under oblique impact at (a) 1073 K,(b) 873K [48].

    5.1. Theoretical aspects

    The details of the interrelationship between erosion conditions

    and erosion mechanisms has been presented earlier. Furtherdiscussion on this interrelationship will be carried outsubsequently. Thus, only the salient theoretical aspects willbe considered in the following section.

    5.1.1. Steady state oxide scale thickness. If it is assumed

    that the oxide scale which forms on the eroding materialduring erosion is adherent and sufficiently ductile to withstandrepeated impacts without developing cracks, steadystateoxidescale thickness can be defined. It can be assumed that theoxidationof theeroding material follows the parabolickineticsgiven by equation (3)

    m2 = Kop t, (3)

    where m is the mass gain experienced by the metal per unitarea due to intake of oxygen to form oxide scale, Kop is the

    parabolic rate constant and t is the time of exposure. Theparabolic rate constant is usually expressed in the form:

    Kop = Ao expQRT

    , (4)

    where Ao is the Arrhenius constant, Q is the activation energy

    for oxidation, R is the gas constant and T is the absolute

    temperature.

    In order to represent EO interaction in mathematical

    terms one needs the rate of growth of the oxide scale thicknesswith time rather than the weight gain given by equation (3).

    As noted by Lim and Ashby [87], once the composition of the

    oxide scale is known, equation (1) can be transformed to give

    Z2 = 2Kpt, (5)

    Kp = 0.5 C2Ko

    p

    , (6)

    where C is a constant for a given oxide composition (unit ism3 kg1). Kp is usually referred to as the scaling constant.

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    Metal

    Deformed

    Region

    Erodent

    Lip

    Lm

    Metal Erosion with No Oxide Scale

    Metal

    Deformed

    Region

    Erodent

    Lip

    Lm

    Metal Erosion with No Oxide Scale

    Metal

    Deformed

    Region

    Erodent

    Lip

    Lm

    Metal Erosion with Thin Adherent Ductile Oxide Scale

    V

    Oxide

    Scale

    Metal

    Deformed

    Region

    Erodent

    Lip

    Lm

    Metal Erosion with Thin Adherent Ductile Oxide Scale

    V

    Oxide

    Scale

    a (Metal Erosion)

    Metal

    OxideZ Lo

    Damaged

    Zone

    V

    Metal

    OxideZ Lo

    Damaged

    Zone

    V

    b (Oxide Erosion)

    Metal

    Deformed

    Region

    ErodentV

    Oxide

    Scale

    Metal

    Deformed

    Region

    ErodentV

    Oxide

    Scale

    Metal

    Erodent

    V

    Oxide

    Scale

    Lip

    Metal

    Erodent

    V

    Oxide

    Scale

    Lip

    Metal

    Composite LayerV

    Metal

    Composite LayerV

    c (Oxidation Affected Erosion)

    Metal

    Oxide

    Scale

    Metal

    Oxide

    Scale

    Metal

    Newly Formed

    Scale

    Metal

    Newly Formed

    ScaleOxide

    Debris

    Oxide

    Scale

    Metal

    Oxide

    Debris

    Oxide

    Scale

    Metal

    d (Oxidation Controlled Erosion)

    Figure 17. Schematic presentation of various erosion mechanisms at elevated temperature.

    A value appropriate to the erosion conditions should be chosen

    for Kp since Levy etal [88] have clearly demonstrated that the

    oxide scales grow much more rapidly under erosion conditions

    as compared with static conditions. From equation (5),

    the rate of increase of oxide scale thickness with time is

    given as

    dZ

    dt=

    Kp

    Z. (7)

    IfEo is assumed to be the erosion rate of oxide scale and

    F be the particle flux rate given by the ratio of particle feed rate

    (f ) to the eroded area then the rate of decrease of the oxide

    scale thickness due to its erosion is obtained as

    dZ

    dt=

    EoF

    o, (8)

    where o is the density of the oxide.

    Finally, a situation will arise when the oxide growth byoxidation (equation (7)) will be equal to the oxide removal by

    erosion (equation (8)). Under such conditions, the steady state

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    a

    Figure 18. Schematic diagrams of various metal removal mechanisms during metal erosion.

    Figure 19. SEM images showing different morphologies of eroded surfaces of Ni exposed at elevated temperature: (a) metal erosion,(b) oxidation affected erosion, (c) oxidation controlled erosion and (d) oxide erosion [67].

    oxide thickness (Zss) can be obtained as

    Zss =Kpo

    EoF. (9)

    Hence, the steady state oxide thickness increases with

    increasing temperature(through Kp), decreasing oxide erosion

    rate and decreasing particle flux rate. It should be mentioned

    that Eo in equation (9) represents theerosion rate of pure oxide.

    5.1.2. Depth of deformed zone in oxide and metal. A largenumber of experiments have consistently shown that the depth

    to which the deformed zone extends is usually of the order of

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    Figure 20. SEM images of the transverse section of the eroded surfaces of Ni shown in figure 19. (a) Metal erosion, (b) oxidation affectederosion, (c) oxidation controlled erosion and (d) oxide erosion [67].

    indentation diameter, or in other words

    L = W , (10)

    where W is the indentation diameter and is a constant of

    the order of unity. The magnitude ofW depends on whether

    the erodent is spherical or angular. When a conical particle

    of mass mp as shown in figure 21 impacts an eroding material

    of hardness H with an impact velocity V, then the incident

    energy of the impacting particle is given as 0.5 mpV2 and the

    energy consumed in forming the crater of volume U is H U

    where H is the hardness of the target material. Equating these

    two energies, we get

    H U = 0.5 mpV2. (11)

    For a spherical erodent having radius r , U is given by

    U = W4

    64r(12)

    since crater depth can be considered to be considerablysmallerthan the diameter of the erodent. Substituting equations (12)

    in equation (11) and solving for W one obtains

    W = 2.56 rV1/2

    H

    1/4, (13)

    where is the density of the erodent. Hence, the depth of

    deformation for a spherical erodent can be obtained by putting

    equation (13) in equation (10) as

    L(Sphe) = 2.56r V1/2

    H

    1/4. (14)

    For conical particles having a half angle of = 30, U is

    given asU =

    24

    W3tan

    . (15)

    Substituting equation (15) in equation (11) and solving for

    W one obtains

    W =2r1/3V2/3

    H1/3. (16)

    Thus the depth of deformation for a conical particle can

    be obtained by putting the value ofW in equation (10) as

    L(con) = 2.0r1/3V2/3

    H1/3. (17)

    Equations (14) and (17) are valid irrespective of whether the

    target material is metallic material or oxide scale. However,

    it should be mentioned that the hardness H in equations (14)

    and (17) represents the hardness of the oxide scale Ho in the

    case of thick oxide scale as target material and the hardness of

    the base metal in cases where the thickness of the oxide scale

    is very small.

    5.1.3. Critical oxide thickness (Zc). An important factor

    that should be considered to understand the EO interactionis that the oxide scale usually exhibits a ductile to brittle

    transition as a function of both thickness and temperature.

    Stephenson et al [89] have demonstrated this phenomenon

    under impact conditions. Saunders and Nicholls [90] have

    also noted similar ductile to brittle transition for chromia and

    alumina coatings. Importantpointsrelated to this phenomenon

    are given as follows.

    (1) At all temperatures, the scale becomes brittle beyond a

    critical thickness (Zc) and thus can be removed easily

    by spalling or by cracking and chipping due to particle

    impacts.

    (2) This value of Zc changes discontinuously over narrow

    temperature ranges usually in the range of 700800

    C.(3) Belowandabovethis temperature range Zc is independent

    of temperature.

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    ts

    /

    Figure 21. Variation of the calculated ratio of the time between impacts to the time of impact with hardness.

    5.1.4. Time between the impacts and time of impact. If a

    spherical erodent of radius r and mass m is considered, then

    the number of particles impacting the unit area of the eroding

    material every second equals F /m where F is the particle feed

    rate. If it is assumed that each impact event causes damage

    over an area A, where A is the impact crater area and is a

    constant of the order of unity, then the number of particles (N )

    impacting an area ofA every second is given by

    N=

    F

    m

    A (18)

    or

    N=

    F

    m

    0.25 W2, (19)

    where A = 0.25 W2, W is the impact crater diameter. The

    time between two impacts can now be obtained as

    tb =4mp

    F W2. (20)

    Substituting the value ofW obtained from equation (13)

    in equation (20) and noting that mp=

    4/3 r3

    , tb is obtainedas

    tb(sph) =0.82r1/2H1/2

    F V. (21)

    In the case of conical particles with a hemispherical top

    of size 2r, mass m and half angle , the time between impacts

    can be obtained from equation (20) if is 30. This is because

    the mass of such a particle is equal to that of a sphere of

    diameter 2r . For conical particles W is given by equation (16)

    and substituting equation (16) in equation (20) and putting

    m = 4/3 r3, tb is obtained as

    tb(con) =4r1/3H2/3

    3F V4/3. (22)

    In the above expression it is assumed that the rebounding

    particle does not interfere with the incident particle. This

    assumption is reasonable because the erosion oxidation

    interaction becomes prominent only at a low particle feed rate.

    It is also important to consider the contact duration

    between the particle and the eroding material during each

    impact. This duration known as time of impact (tim) is given

    as [91, 92]

    tim(sph) =1.28r

    H1/2, (23)

    where r is the radius of the spherical particle having hardness

    H and density . Thus for spherical particles the ratio of

    time between impacts and time of impact can be obtained by

    dividing equation (21) by equation (23) as

    tb

    tim(sph) =

    0.64H

    V F. (24)

    In the case of conical particles the time of impact can be

    given to a good approximation as

    tim(con) =2.8r1/3

    H1/3V1/3. (25)

    Thus the ratio oftim and tb is obtained from equations (22)

    and (25) as

    tb

    tim(con) =

    0.48H1/3

    V F. (26)

    In the above equations H represents the hardness of the

    eroding material. The calculated values of the ratios tb/tim in

    the case of spherical (continuous lines) and conical erodents

    (broken lines) are illustrated in figure 21 as a function of

    hardness of the eroding material and for four values of the

    product of impact velocity and feed rate. It can be noted from

    figure 21 that the time between impacts is several orders of

    magnitude higher than the time of impact. Hence for theerosion process at elevated temperature, time of impact has

    negligible influence compared with time between impacts.

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    5.1.5. Oxide scale growth between impacts. On the

    assumption that oxidation is governed by a parabolic law,

    the growth of oxide scale thickness (Z) is described by

    equation (5). Thus the thickness of the oxide scale (Zb) grown

    between two successive impacts is given by

    Z2b = 2Kptb. (27)

    Substituting the value oftb from equations (21) and (22)

    in equation (27), one obtains the following equation for Zb for

    spherical and conical particles.

    Zb(sph) = 1.26

    Kpr

    V F

    1/2(H)1/4 (28)

    and

    Zb(con) = 1.63Kpr

    F

    1/2

    1/6H1/3

    V2/3 . (29)

    While deriving the above two equations it is assumed

    that the growth of the oxide scale is controlled by the metal

    and/or the oxygen ion diffusion through the scale. Thus, it

    is assumed that the oxide scale does not crack as it grows,

    thereby providing an easy path for the oxygen diffusion to

    the metal oxide interface. This assumption is reasonable

    because it concerns the growth of the oxide scale at a very local

    region surrounding the impact point wherein prior impact has

    removed the scale. Thus, the scale needs to be adherent and

    uncracked only in this local region for the parabolic kinetics

    to be valid. It does not matter that the scale is heavily cracked

    or spalled at the macroscopic level.ThemagnitudeofZb incomparisonwithsteadystateoxide

    scale thickness (Zss) has an important bearing on the erosion

    oxidation interaction. Therefore, the variation ofZss and Zbwith impact velocity is given in figure 22 for two different

    temperatures and two different feed rates. The magnitude of

    Zb is indicated for both spherical and conical erodents. The

    values of various parameters used for calculating Zb and Zssare given in table 3. Since most of the work on elevated

    temperature erosion is done with steel, the values appropriate

    to steel are chosen for various parameters. A value of 105 for

    Ao and 210kJ mol1 for Q are chosen on the basis of the data

    reported by Quinn [93]. The value ofC is calculated based

    on the formation of Fe2O3 scale as observed by Levy and co-

    workers [29, 45, 59] for a variety of ferritic steel undergoing

    erosion oxidation degradation. The hardness of the oxide

    scale and the metal is assumed to be 3.0 GPa and 2.0GPa,

    respectively. Zc iskeptwithintherangeof110 m, consistent

    with values reported by various investigators [89, 90]. A

    perusal of the erosion literature indicates that the particle feed

    rate mostly lies in the range 0.110 kg m2 s1. The erosion

    rate of the oxide scale is assumed to be proportional to V3. The

    test temperature is chosen in the range of 8731173 K since the

    oxidationeffect becomes importantat these temperaturesin the

    case of steels. It is clear from figure 22 that Zss decreases much

    more rapidly with impact velocity than Zb. Thus a transitionvelocity beyond which Zss < Zb can be obtained for a given

    temperature and feed rate.

    Table 3. Assumed values of various important parameters.

    Constant/variable Symbol Values Units

    Hardness of oxide Ho 3.0 GPaHardness of metal Hm 2.0 GPaParabolic rate constant Kop kg

    2 m4 s1

    Arrhenius constant Ao 105, 104, 103 kg2 m4 s1

    Activation energy Q 210 kJ mol1

    Erosion rate of oxide Eo kgkg1

    Erosion rate constant Eoo 105107

    Reference velocity Vo 10 m s1

    Velocity exponent n 3Density of oxide o 5400 kg m

    3

    Density of particles p 3200 kg m3

    Erodent radius r 100(10) mCoversion factors for C 1.3 104 m3 kg1

    transforming Kop to KpParticle flux rate F 0.1, 1.0, 10.0 kgm2 s1

    Particle shapeCritical oxide thickness Zc 1, 10 mImpact velocity V 5100 m s1

    Test temperature T 8731173 K

    5.2. Conditions for prevalence of various EO mechanisms

    If there is no oxide scale on the metal surface or if the

    thickness of the oxide scale is very small compared with the

    depth to which the deformation extends in the metal surface,

    the dominant erosion mechanism will be metal erosion. On

    the other extreme, if the steady state thickness (Zss) of the

    oxide scale is less than the critical thickness of spalling (Zc)

    and the depth of deformation is lower than the steady state

    thickness, oxide erosion is the prevalent erosion mechanism.

    If, however, Zss is lower than Zc and the depth of the

    deformed zone is bigger than Zss, the oxidation affectederosion mechanism is observed. Finally, if the steady state

    thicknessof theoxidescaleis greater than thecriticalthickness,

    the oxide scale will never attain steady state thickness. The

    erosion will take place by spalling of the scale and oxidation

    controlled erosion will be operative.

    Roy et al [94], employing a new methodology, examined

    thetransitioncriteria from themetalerosionregimeto theoxide

    erosion regime. In their work, they eroded pre-oxidized Ni

    samples having varying thicknesses of oxide scale at ambient

    temperature. The ratio of the erosion rate of the oxide scale

    (Eo) to the erosion rate of the substrate (E) is plotted against

    the ratio of the initial thickness of the oxide scale (t) to the

    depth of deformation (L) due to impact. Their observationis portrayed in figure 23. This figure reveals three distinct

    regimes. In region one, the value oft/L is higher than 4.0.

    The erosion rate of the oxide scale assumes a relatively high

    but constant value. In region two, t /L is higher than 0.5 but

    lower than 4.0. In this regime, there is a smooth change of the

    relative erosion rate from a low value to a high value. Finally,

    in regime three, t/L is lower than 0.5. In this regime, the rate

    of change of the relative erosion rate is slow. In addition, there

    appears tobea peak in therelative erosion rate atapproximately

    t /L = 6.

    Regime one can be deduced as an oxide erosion regime

    on the basis of the erosion response, which is brittle, i.e.

    higher erosion rate at normal impact and on the basis of thevelocity exponent, which is 3.0, of the erosion rate. Further,

    the material in this regime was removed by brittle chipping.

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    Figure 22. Variation of the calculated values of the steady state thickness and the thickness of the oxide scale grown between two successiveimpacts.

    Figure 23. Variation of the ratio of the erosion rate of the oxide scale to the erosion rate of the substrate with the ratio of the thickness of theoxide scale to the depth of deformation [94].

    In contrast, regime three is characterized by pure metallic

    erosion because the thickness of the oxide scale wasnegligibly

    low. In addition, the erosion response, the material removal

    mechanisms and the velocity exponent of the erosion rate in

    this regime are consistent with those of the erosion of metals

    and alloys at ambient temperature. Regime two represents the

    transition from the oxide erosion regime to the metal erosion

    regime. It also shows that the transition is not sharp but rather

    smooth. Thus as long as the depth of deformation is confined

    within the oxide scale, erosion takes place from the oxidescale only and erosion behaviour similar to oxide erosion is

    prevalent. When there is no oxide scale, metal erosion is

    dominant. In the intermediate regime, erosion may take place

    from the oxide layer, but the deformation will extend to the

    substrate also.

    5.3. Models for erosion oxidation interaction mechanisms

    Several investigators [57, 61, 95103] have tried to identify

    various possible mechanisms of interaction between erosion

    and oxidation over the last few years. For example,

    Hogmarketal [95] have identified six differentmechanismsof

    interaction ranging from pure oxidation to pure erosion. Suchmechanisms are compiled in the report of Stack et al [96]

    and Sundararajan and Roy [16]. Wellman and Nicholls [97]

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    presented an excellent review on this aspect. Barklow and

    Petit [98] have identified four different mechanisms such as

    metallic erosion, oxidation modified erosion, erosion modified

    oxidation and oxidation on the basis of the combined effect of

    kinetic energy of the impacting particles, oxide growth rate

    and particle flux rate. According to them the effect of thesubstrate becomes negligible when the particle impact energy

    and particle flux rate are less. The influence of the substrate

    becomes important at high particle flux rate and high impact

    energy. Wright et al [52] classified the interaction between

    corrosion and erosion into two regimes on the basis of kinetic

    energies of the impacting particles. When the kinetic energy

    is low, erosion behaviour exhibits brittle erosion mechanisms

    characterized by a maximum erosion rate under normal impact

    and a velocity exponent in excess of 3.0. When the kinetic

    energy is high, erosion behaviour is ductile, maximum erosion

    rate occurs at oblique impact angle and the velocity exponent

    lies in the range 22.5. This classification was subsequently

    modelled by Natesan and Liu [99] and later modified byStacket al [100].

    Rishel et al [101] extended the idea originally proposed

    by Kang et al [50] and Chang et al [102]. They defined

    various mechanisms of erosionoxidation interaction using four

    parameters: instantaneous scale thickness ( ), parabolic rate

    constant under combined attack of erosion and oxidation Kce,

    erosion rate constant of oxidation product K and parabolic

    rate constant for oxidation (Kp) only. According to these

    investigatorstherateof change of instantaneous scalethickness

    is given byd

    dt=

    K(ce)

    K . (30)

    If d /dt is positive erosion of the oxide scale takes place.Erosion under such conditions will be characterized by a brittle

    erosion response. If d/dt is negative oxidation affected

    erosion becomes dominant, i.e. erosion takes place from a

    composite layer consisting of oxide scale, metallic substrate

    and erodent. If, however, d /dt is equal to zero erosion

    enhanced oxidation plays a dominant role. Within this regime

    three different modes are possible; Type I erosion enhanced

    oxidation will be operative if K(ce) is equal to Kp. Type II

    erosion enhanced oxidation can be seen ifK(ce) is greater than

    Kp and Type III erosion enhanced oxidation occurs when the

    oxide scale spalls. Finally, if there is no corrosion, metal

    erosion will be prevalent. This model, in principle, canexplain

    the effect of feed rate, particle size, etc on the observed erosionrate. However, the predictive capability of this model is

    limited.

    Sethi and Corey [54], with the help of oxide scale growth

    kinetics, have demonstrated that the temperature dependence

    of erosion rate shows three different regimes. These regimes

    are (1) a low temperature regime where erosion rate is

    independent of temperature, (2) an intermediate temperature

    regime where erosion rate increases with the increase of

    temperature and (3) a high temperature regime.

    Stephenson and Nicholls [103] have defined three

    different regimes on the basis of the ratio of contact radius (a)

    and scale thickness (z). If this ratio is less than 0.1 a substrate

    dominated regime can be seen. If this ratio is between 0.1and 1.0, oxide modified behaviour will be prevalent. If this

    ratio is more than 1.0 oxidation dominated erosion will be the

    operatingmechanism. Theyalso proposed the presenceof pure

    oxidation in the case of the negligible presence of the erodent.

    Another classification due to Stacket al [104] proposes

    the presence of three regimes, namely, erosion dominated,

    erosioncorrosiondominated and corrosion dominated. These

    regimes are defined based on kinetic energy, temperature andcritical oxide thickness. The transition to corrosion dominated

    behaviour can be attributed to the formation of critical oxide

    thickness. Above the temperature at which this occurs, the

    oxide formed in a given time interval cannot be removed from

    the scale metal interface by erosion. Below the temperature at

    which the critical scale thickness is attained, the oxide formed

    can be removed during impact. The corrosion dominated

    regime can be further divided into two more sub-regimes

    depending on the velocity dependence of these regimes. The

    corrosion dominated regimes can be corrosion dominated-1

    and corrosion dominated-2 regimes. In the processes of

    identifying these mechanisms, Stack assumed that oxidation

    behaviour of the target material follows a parabolic oxidationbehaviour and the oxidation that occurs during each impact is

    negligible.

    Sundararajan [78] has broadly proposed two differ-

    ent regimes of EO interaction, namely, erosion controlled

    regimes and oxidation controlled regimes. In erosion con-

    trolled regimes three different mechanisms can be envisaged.

    These mechanisms are(a)metal erosion, (b)oxidationaffected

    erosion and (c) oxide erosion. In oxidation controlled regimes

    there are two different mechanisms, namely (a) oxidation con-

    trolled erosion continuous and(b) oxidation controlled erosion

    spalling. These zones can be identified on the basis of sev-

    eral erosion related parameters. The most important feature of

    this model is the ability of the model to predict the prevalentmechanisms of erosion once the conditions of erosion and the

    thermo-physical properties of the erodent and target material

    are known.

    5.4. Erosion oxidation interaction map

    While establishing the operative mechanisms for erosion

    oxidation, it is noted that erosion conditions significantly

    influence the oxidation. The factors which influence the

    operating mechanisms are impact velocity, impact angle, feed

    rate and temperature. Similarly, the particle size and shape

    also have a profound effect on this map. The combined

    influence of all these factors on erosion rate remainedqualitative for a considerably long time. Specific erosion

    mechanismsfor variousmetallic materialshave beendescribed

    by Hogmark et al [95], Wright et al [52], Kang et al

    [50] and Sundararajan [78]. Barkalow and Petit [98] for

    the first time have tried to organize such information in the

    form of an erosion oxidation map where the prevalence of

    various mechanisms is shown in the domain of the particle

    kinetic energy and the scale growth rate. Sundararajan [78]

    has attempted to organize erosion oxidation maps in the

    domain of impact velocity and temperature. Stephenson

    and Nicholls [77, 105] have plotted particle velocity versus

    oxide thickness for a specific particle size and temperature

    to construct such maps while Stack and Pena [106] plottedvelocity versus temperature. But the attempt has remained

    limited with the consideration of theoretically postulated

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    values of erosion rates. Numerous experiments conducted

    by the author can be considered sufficient to attempt making

    erosion oxidation interactionmapsfrom the experimental data.

    Because of the significance of various erosion conditions

    on erosion rate and erosion mechanisms, an erosion oxidation

    interaction map can be represented in a multidimensionalconfiguration. A simplified representation of the erosion

    oxidationmap canbe made in a two-dimensionalplot of impact

    velocityand temperature fora givenimpact angle andfeed rate.

    The influence of feed rate on the EO map at normal impact

    for commercially pure Ni is shown in figure 24 whereas the

    influence of impact angle on the EO map of Ni is illustrated

    in figure 25. Similarly the effect of Cr addition on the EO

    map can be noted in figure 26. In general all these maps

    describe the transitional boundary between regimes of various

    operative mechanisms of erosion at elevated temperature.

    These maps are able to clearly delineate the metal erosion,

    oxidation affected erosion, oxidation controlled erosion and

    oxide erosion. The extent of each of these regimes depends ontemperature, feed rate, impact angle and impact velocity. An

    examination of all these maps shows that:

    (a) a low temperature imparts the metal erosion regime. With

    an increase in temperature the metal erosion regime shifts

    to the oxide erosion regime via the oxidation affected

    erosion and oxidation controlled erosion regimes,

    (b) a higher feed rate extends the metal erosion regime and in

    turn alters theexistence andtheextentof theother regimes

    and

    (c) oblique impacts tend to reduce the extent of the metal

    erosion regime and promote other regimes.

    Theexistence andextent of a particular regime is governedby the oxide scale growth and the depth of deformation due to

    impact. These two factors are opposing in nature with respect

    to erosion conditions. Thus for a given condition, keeping

    the impact velocity constant, as the temperature of erosion is

    increased, the influence of oxide scale becomes dominant. As

    a result, the oxide scale starts growing at a rate faster than

    erosion. This leads to a situation where the thickness of the

    oxide scale becomes significant compared with the depth of

    deformation andat still highertemperaturewhere thethickness

    of the scale attains critical thickness of spalling or attains a

    thickness where the rate of growth of oxide scale is equal to

    therate of erosion. This results in transition from metal erosion

    to oxidation affected erosion or oxidation controlled erosionor even to oxide erosion. This can be seen in figure 25 at

    impact angle of 30 and at impact velocity of 35 m s1 and at

    feed rate of 0.2 g min1. Similarly keeping the temperature

    of erosion constant as the impact velocity is increased, it not

    only becomes more difficult for the oxide scale to grow but the

    thickness of the oxide scale also becomes less compared with

    the depth of deformation. This situation causes prevalence of

    metal erosion in preference to oxidation affected erosion and

    oxidationaffectederosion in preferenceto oxidationcontrolled

    erosion, as shown in figure 24 (at impact angle of 90, feed rate

    of 0.2 g min1 and temperature of 673 K).

    The effect of the higher particle feed rate is analogous

    to that of lower temperature. At a specific condition, higherparticle feed rate does not permit the oxide scale to grow as the

    time intervals between impinging particles are shortened. This

    (a)

    (b)

    Figure 24. Erosion oxidation interaction map for Ni, (a) for feedrate of 3.3 106 kg s1 and (b) for feed rate of 3.3 104 kg s1.

    condition results in an expansion of the metal erosion regime

    and the shifting of other erosion regimes to higher temperature

    or lower impact velocities. The effect of impact angle can

    be considered in terms of impact velocity. As the impact

    angle isdecreasedthe normalcomponent of theimpact velocitydecreases. Thus, oblique impact gives rise to constricted metal

    erosion regimes. Consequently, the oxidation affected erosion

    regime and the oxidation controlled erosion regimes appear at

    higher impact velocity and lower test temperature. At oblique

    impact, it is possible to seethe presence ofoxideerosion, which

    is not prevalent at normal impact in many cases.

    It is noted in figures 2426 that the erosion rate tends

    to increase and the erosion oxidation interaction mechanism

    shifts from metal erosion to oxide erosion via oxidation

    affected erosion and oxidation controlled erosion with the

    increase of temperature. It can also be inferred that the erosion

    rate is higher (1) in oxidation affected erosion than in metal

    erosion, (2) in oxidation controlled erosion than in oxidationaffected erosion and (3) in the oxide erosion regime than in the

    oxidation controlled erosion regime [107]. It is important to

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    (b)

    (a)

    Figure 25. Erosion oxidation interaction map for Ni, (a) for impactangle of 30 and (b) for impact angle of 90.

    mention that the erosion oxidation map has been constructed

    experimentally for the first time. The influence of various

    erosion conditions on such a map can be explained on the basis

    of oxidation characteristics and mechanical properties of theeroding materials. Stacket al [108] constructed a similar map

    previously. However, such a map was available only in the

    low velocity regime. It also failed to highlight the influence of

    other parameters such as particle feed rate, impact angle, alloy

    composition, etc.

    6. An analysis of enhanced oxidation kineticsdue to erosion induced roughness

    The oxidation kinetics of metals and alloys are found to

    alter during erosion or wear. The observation on enhanced

    oxidation kinetics is primarily centred on iron base alloys. The

    influence of sliding wear on oxidation was initially proposedby Quinn [109]. According to Quinn, the activation energy

    for the parabolic rate constant (KP) remains the same during

    (a)

    (b)

    Figure 26. Erosion oxidation interaction map for (a) Ni and(b) Ni20 Cr alloy.

    static or wear induced oxidation. However, the magnitude

    of KP of wear induced oxidation is higher than that for

    static oxidation. A similar contention is also made by Lim

    and Ashby [87] for wear induced oxidation and by Levyand co-workers [29, 45, 59] for erosion induced oxidation.

    Roy et al [76] for the first time attempted to estimate the

    altered oxidation kinetics during erosion and subsequently

    tried to formulate a phenomenological model to explain such a

    result.

    The observations of Roy et al [76] are presented in

    figures 27 and 28. The variations of mass gain per unit area

    as a function of time at 1073 K for as-received and eroded Ni

    are given in figure 27 whereas figure 28 depicts similar data at

    1173 K for Ni20Cr alloy. It is clear that the oxidation rate of

    Ni increases significantly for eroded samples when compared

    with as-received samples. The oxidation rate increases with

    the increase of impact velocity. The increase of oxidation ratewith increase of impactvelocityis higherat normalimpactthan

    at oblique impact. With regard to the Ni20Cr alloy it is noted

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    0.000

    0.001

    0.002

    0.003

    0.004

    0.005

    0.006

    0.007

    0.008

    0 10 000 20 000 30 000 40 000 50 000 60 000 70 000 80 000

    Time (sec)

    MassGain/UnitAreax103 (Kg/m

    2)

    As Received

    V = 35 m/s, = 30oV = 65 m/s, = 30oV = 35 m/s, = 90oV = 65 m/s, = 90o

    Material: Ni

    V= Impact Velocity

    = Impact AngleTemperature : 1073 K

    Figure 27. Variation of mass gain per unit area of Ni with time at 1073 K [76].

    0

    2

    4

    6

    8

    10

    12

    14

    16

    18

    0 10 000 20 000 30 000 40 000 50 000 60 000 70 000 80 000

    Time (sec)

    MassGainperU

    nitAreax103

    (Kg/

    m2)

    Material: Ni-20Cr

    V= Impact Velocity

    = Impact AngleTemperature : 1173 K

    As ReceivedV = 35 m/s, = 30 oV = 65 m/s, = 30 oV = 65 m/s, = 90 oV = 35 m/s, = 90 o

    Figure 28. Variation of mass gain per unit area of Ni20Cr alloy at 1173 K [76].

    that the oxidation rate decreases with the increase of impact

    velocity. Further, the influence of impact angle on oxidation

    kinetics is negligible.

    Theabove observation forNi is modelled by assuming that

    the parabolic rate constant is related to the surface roughness

    (Ra) or impact velocity as

    K = KO1(Ra)x1 exp

    Q

    RT

    , (31)

    K = KO2 (V sin )x2 exp

    Q

    RT , (32)

    where KO1 and KO2 are constants, V is the impact velocity and

    is the impact angle, Q is activation energy, R is the universal

    gas constant, T is test temperature andx1and x2 areroughness

    exponent and velocity exponent, respectively. In order to

    establish the relation between the parabolic rate constant

    and impacting condition, the average activation energy for

    the parabolic rate constant is determined by plotting ln K

    (parabolic rate constant) against (1000 T1) i n K1. Using the

    average activation energy, the average parabolic rate constants

    at different eroding conditions are estimated. The natural

    logarithm of the average parabolic rate constant is then plotted

    against ln Ra and ln V sin . The slopes of best-fit straight

    lines are then computed as constants KO1 and KO2 whereasthe intercepts of the lines with the ordinate are calculated as

    exponents x1 and x2. The expressions for rate constants are

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    y

    Figure 29. Variation of the parabolic rate constant with (V sin )2.08

    exp(Q/RT ) [76].

    then obtained as

    K = 4.67 109(V sin )2.08 exp

    22 400

    RT

    , (33)

    K = 9.62 107(V sin )4.26 exp

    22 400

    RT

    . (34)

    In order to assess the ability of the expression to predict

    the parabolic rate constant, the estimated rate constants are

    plotted against (V sin )2.08

    exp(22 400/RT ) in figure 29.A straight line with a good fit suggests the suitability of the

    expression.

    A similar exercise cannot be carried out for Ni20Cr

    alloy because of two factors. First, the nature of the oxide

    scale that forms on Ni20Cr alloy can have a dual grain size

    distribution [110]. Second, higher roughness in these alloys

    results in lower sizes of the globular oxide grains. Hence even

    though the roughness changes the amount of grain boundary

    also gets altered and this in turn provides different extents of

    short circuit paths. Thus the pre-exponential factors in the

    Arrhenius type equation should be a function of the roughness,

    grain size and the nature of the oxides that are present in the

    oxide scales of Ni20Cr alloy. Hence a similar modelling forNi20Cr alloy cannot be achieved.

    7. Areas of future research

    In spite of significant progress in elevated temperature erosion

    of metals and alloys, certain areas still need to be addressed.

    The material flow behaviour during solid particle erosion is at

    high strain, high strain rate, under adiabatic deformation and

    undermultiaxial stress condition. The material flow behaviour

    under such conditions, particularly at elevated temperature is

    not well understood. The estimation of mechanical properties

    of materials under such conditions is required for effective

    modelling of the elevated temperature erosion behaviour ofmaterials. Thus there is a clear need to develop a simplified

    test technique which will simulate the erosion conditions in a

    test sample and evaluate the mechanical behaviour under such

    conditions. For example the depth of deformation estimated

    using equation (14) would be more accurate if dynamic

    hardness is used instead of static hardness.

    The deformation and fracture behaviour of the oxide scale

    under erosion conditions is poorly understood. Further, thehigh strainrate flow behaviour of a layered structurecontaining

    the oxide scale and the substrate material also needs to be

    addressed. Such an understanding is required to model the

    spalling behaviour of theoxide scale once it reaches thecritical

    thickness of spalling. The dramatically different spalling

    behaviour of the segmented scale and the compacted scale can

    be explained more accurately only when concepts related to

    such deformation behaviour get crystallized.

    The kinetics of oxidation during erosion are an order of

    magnitude higher than that under static conditions. An effort

    to estimate the increased oxidation rate quantitatively either

    through careful experiment or by rigorous theoretical analysis

    is hitherto unexplored. All the reasons for such acceleratedoxidation are not yet revealed. Thus, there is a clear need

    to carry out organized experiments to evaluate the oxidation

    behaviour of materials under erosion conditions. Attempts

    should be made to separate out the influence of possible factors

    responsible for enhanc