A Case Study of Stainless Steel Water Supply Pipe Corrosion Caused by Weld Heat Tint

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    A CASE STUDY OF STAINLESS STEEL WATER SUPPLY PIPECORROSION CAUSED BY

    WELD HEAT TINT

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    Amongst

    several techniques, pickling using a mixture of HF and HNO

    3

    acid has been found to be the most

    effective method[7, 9 11]. However, pickling is not always possible due to safety issues,

    cost andaccess. Such problemsaremore prominent for site-welded stainless steel systems as it is

    relatively

    easier to control welding parameters and pickling processes in the workshop. Thus, it is

    important

    that end users and fabricators have a better understanding of the effect of heat tint on

    localised

    corrosion for stainless steel systems and its working environment. An agreement on

    acceptableheat tint level should be finalised between fabricators and end users prior to

    manufacturing and it should be welldocumented.

    An acceptable heat tint level can be determined by heat tint colour reference charts, such asAmerican Welding Society Standards AWS D18.1/D18.1M (2009) [12] and AWS D18.2

    (1999) [13]

    or Force charts Nos. 1 -5 (The Force Institute, Denmark) [14]. For austenitic stainless steel

    (e.g.

    AISI Types 304 and 316) welds used in food, dairy and pharmaceutical industries, both

    colour

    charts suggest that the acceptable heat tint level should not go beyond grey or straw yellow

    (e.g.

    brown, blue or black). Above this level, the weld may be susceptible to localised corrosion

    attack.

    When unacceptable heat tint is unavoidable and pickling is not an option, fabricators and end

    users should consider carrying out corrosion tests on welded samples to determine if the weld

    quality willmeet the design specification.

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    (

    b)

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    Figure 3: Internal views of pipes with weeping issue. (a) Shorter pipe with butt weld;large

    corrosionnodules were observed at the weld root.(b) Longer pipe with weeping along the pipe length.

    The

    location of the suspected seam weld is indicated.

    The corrosion product nodules were found to be quite porous and fragile (Figure 4a) and

    some

    large pits were observed underneath the corrosion products (Figure 4b).

    Figure 4: Detailed views of corrosion product nodules and underlying metal appearance. (a)

    Porous corrosion product nodule formed on the ID surface of a longer pipe sample and (b) pit

    (~ 0.75 mm in diameter, arrowed) observed underneath the corrosion product from the ID

    surface

    of a shorter pipe sample.

    Localised areas associated with the pitting at the pipe inner surface were cleaned using a

    cotton

    swab doused in isopropanol. In both cases of pitting associated with a butt weld and along a

    suspected seam weld, a dark brown coloured heat tint was identified (see Figure5). The heat

    tint

    also confirmed the presence of a seam weld in the longer pipe section samples.

    Several metallurgical samples were removed across the pitting damaged area including

    associated

    weld from both short and long pipe section samples. In each case, significant pitting was

    observed

    adjacent to the weld (i.e. in the parent metal or heat affected zone) just beneath the pipe inner

    surface,with the largest pit sampled having progressed almost entirely across the pipe

    wall. No

    pitting of the weld metal was identified. The corrosion products formed above and within thepit

    were porous and possibly multiphase. A typical example of the pitting damage is shown in

    Figure 6.

    (a)

    (b)

    Suspected seam weld

    (a)

    (b)

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    Figure 5: Appearance of (a) pipe with butt weld and (b) pipe with suspected seam weld afterlocalised cleaning about the pitting regions. In both instances a heat tint (arrowed; dark

    brown

    discoloured region) was identified.

    Figure 6: Macrograph showing a typical cross-section view of pitting damage near the weld.

    Sample sectioned from a longer pipe sample with seam weld. Marker division in mm.

    2.2

    Root cause of the failure

    Examination of the supplied pipe samples revealed that weeping was caused by pitting

    damage

    initiated from the pipe ID at weld heat tint regions. Crevice corrosion attack initiated at the

    weld

    heat tint regions and progressed further as pitting corrosion. The species responsible for

    crevice

    and pitting corrosion is usually chloride ions; these can penetrate the passive film that

    stainless

    steels rely on for their excellent corrosion properties. The action of the ions cause local

    destruction

    of the passive film and prevents repassivation, allowing rapid dissolution of the metal to

    proceed.

    The resistance to pitting and crevice corrosion is related, and for Type 304 and 304L,

    adequate

    pitting resistance is expected when fully immersed in domestic water containing < 200

    ppm Cl

    -

    from ambient up to 95C [15]. Potable water typically contains chloride concentrations of

    10 to50 ppm [16]. If the chloride concentration of the plant water supply was maintained at these

    levels,

    it is unlikely Type 304L piping would suffer corrosion. However, the presence of the heat

    tint has

    compromised the corrosion resistance of the piping at the welds in this instance, leading to

    significant localised pitting and eventual pipe leaking.

    (a)

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    (b)

    Weld

    Pipe ID surface

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    3

    PITTING CORROSION TESTING OF WELD SAMPLES FROM A WATER

    RECYCLING

    PLANT

    3.1

    Background of the testing

    During the construction of a water recycling line in the same dairy plant, a portion of site-

    welded

    Type 316 pipe was inspected with radiography testing (approx. 80 welds in total). A

    number of

    locations were found to be oxidised due to insufficient purging of the ID surface.In total,a

    near

    continuous heat tint was observed on seven welds and isolated oxide film was found on

    anothertwelve welds. In order to determine the quality and suitability of these welds, two welds were

    submitted for pitting corrosion testing using ASTM G48 03 [17], to reveal locations

    susceptible to

    pitting corrosion.

    The as received pipe samples are shown in Figure 7. Both samples were in the as-welded

    condition without passivation. Samples were cut to expose the interior appearance of the

    circumferential welds. Insufficient purging during welding had led to the development of a

    heat tint

    film with various colours ranging from dark blue to dark brown near the weld (Figure 7b). At

    the

    weld root, defects such as corrosion, lack of fusion and undercut were observed. A detailed

    view of

    these defects is seen in Figure 8a. Slag inclusions could be found in the weld metal in some

    locations and a typical example from the large pipe is shown in Figure 8b.

    Figure 7: Photographs showing the weld samples submitted for corrosion testing.

    Figure 8: Photographs showing the weld defects observed from both the internal and external

    surface of the pipe.

    (a)

    (b)

    (a)(b)

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    3.2 Experimental

    A total of eight samples (four samples from each pipe) were removed for testing at 22C and

    55C

    (i.e.the typical temperature range that these pipes would be exposed to during service). Theedges

    of each sample were ground with 120-grit abrasive paper as instructed in ASTM G 48 03.

    Half of

    the samples were tested in the as-received condition and the other half were tested after

    carrying

    outa passivation treatment as specified by the fabricator:

    Passivation Procedure:

    Pre-rinse the samples with water.

    Make-up a 3% caustic solution and heat the solution to 60C. Rinse the samples with

    the caustic solution till clear.Make-up a 4% nitric solution and heat the solution to 45C. Rinse the samples with the

    acid solution for 60 minutes till clear.

    Clean the samples with acetone in an ultrasonic bath before use.

    It was observed that the heat tint was not removed after this passivation process.

    The samples were exposed to a chloride-containing solution, which is expected to be similar

    to the

    condition within a pit or crevice site on ferrous alloys within a chloride-bearing environment

    [14]. As

    instructed in ASTM G 48 03, Method A, a 6% FeCl

    3

    (by mass) solution was made (i.e. 100g of

    reagent grade ferric chloride, FeCl

    3

    H

    2

    O in 900 ml of Type IV reagent water). Sample strips were

    then immersed in the above solution for up to three days at the test temperatures.The test

    solutiontemperature was controlled by a water bath.

    3.3 Results

    The results after the exposure tests are summarised in Table 1. Weight loss was observed in

    all

    specimens, indicating pitting corrosion had occurred in all tests.

    Table 1: Summary of pitting corrosion testing results.

    Day 1Day 2

    Day 3

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    Pitting Depth

    (mm)

    Pitting Depth

    (mm)

    Pitting Depth

    (mm)Sample ID

    &

    Condition

    Weight change

    (mg/cm

    2

    )

    Max. Ave.

    Weight change(mg/cm

    2

    )

    Max.

    Ave.

    Weight change

    (mg/cm

    2

    )

    Max. Ave.

    1 P

    -0.4762 0.114

    0.033 -0.747 1.072

    0.310 -1.087 1.470

    0.870

    2 A -0.4627 0.416

    0.144 -0.689 1.465

    0.396 -1.090 1.465

    0.996

    3 P

    -0.6505 0.9400.429 -1.150 1.480

    1.041 -1.657 1.480

    1.242

    4 A

    -0.75 0.993

    0.846 -1.089

    1.085

    0.926 -1.659 1.486

    1.131

    5 P

    -0.4298 0.0640.022 -0.829 0.641

    0.181 -1.312 1.517

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    0.610

    6 A -0.407 0.941

    0.046 -0.679

    0.208

    0.130 -1.043 0.658

    0.5737 P

    -0.7745 1.408

    0.970 -1.476 1.497

    1.254 -1.943 1.510

    1.406

    8 A

    -0.76 1.136

    0.761 -1.473

    1.444

    0.794 -2.064 1.520

    1.049

    : A - Passivated, P -As received

    3.3.1 Ferric chloride pitting testing at 22C

    For specimens exposed at 22C for 24 hours, specimens with the passivation treatment

    exhibited

    a better pitting corrosion resistance than the as-received specimens (Figure 9), i.e. less and

    shallower pits were formed on the passivated specimens. Most of the pits were located in the

    parent metal (PM) near to the heat tint patches.

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    - 8 -

    Figure 9: Photographs of (a) sample 5 (passivated) and (b) sample 6 (as-received) after oneday

    exposure. The pits were concentrated near the heat tinted area as indicated (circled).

    The severity of the pitting damage increased with increasing exposure time. In all tests, the

    passivated specimens exhibited better pitting corrosion resistance than the as-received

    specimens.

    3.3.2 Ferric chloride pitting testing at 50C

    The pitting damage,in terms of size and depth of pits, was found to be more severe at 50C

    compared to the 22C exposure tests. As with the 22C exposure tests, most of the pits werefound in the PM near to the heat tint patches. Again, passivated samples exhibited better

    pitting

    corrosion resistance than samples inthe as-received condition.

    3.4 Discussion

    Both submitted pipes exhibited various weld defects such as corrosion, slag inclusions, lack

    of

    fusion and undercut at the weld root. These defects create ideal sites for pitting since the

    diffusion

    of oxygen is very limited in these sites. In long term service, debris is more likely to be

    caught

    along the weld. This will lead to the accumulation of debris which provides more favourable

    sites

    for pitting corrosion.

    It was found that the current cleaning and passivation process was insufficient, i.e. the

    heat tint

    was not adequately removed under the current passivation process. During pitting corrosion

    tests,

    most of the pits in the PM were found to have initiated near the heat tint patches. This can beexplained by the crevice/pitting corrosion mechanism described in Section 1. It is widely

    accepted

    that the heat tint film on the stainless steel surface and the underlying chromium depleted

    material

    should be removed using a mechanical method or a pickling treatment before passivation. In

    the

    case of insufficient pickling, the subsequent passivation treatment will not be able to

    build the

    desired passive layer and pitting corrosion will occur in the area with heat tint.

    As a result of the pitting corrosion testing and analysis, it was recommended that the currentdegreasing and passivation treatment be reviewed, and that a pickling treatment be included

    prior

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    to passivation.It was also recommended that the welding procedure and welding records be

    reviewed to ensure appropriate weld quality is achieved.

    4 CONCLUSIONS

    The heat tint formed on stainless steel during welding, cutting and other fabricatingprocessescan

    significantlyreduce theresistance to pitting and crevice corrosion. Fabricators and end users

    should

    be aware of the potential impact of heat tints on welded stainless steel components, and use

    appropriate preparation, purging during welding, descaling/pickling and passivation

    treatments.

    Post weld cleaning of heat tint using either a mechanical method orpicklingtreatment removes

    weld

    scale and heat tint, while a passivation treatment restores the passive film for optimum

    corrosionresistance. However, welding carried out on-site may not allow these practices due to safety

    and

    access issues. In this case, both the fabricator and end user should consider the exposure

    environment and agree on an acceptable heat tint level and ways to achieve this.

    (a)

    (b)

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    - 9 -

    Although ASTM G 48 03, Method A is designed for evaluating pitting

    corrosion resistance in

    chloride-bearing environments, it can be used to evaluate the potential for pitting damage and

    effectiveness of post-weld cleaning.

    REFERENCES:

    [1]. S. turner, F.P.A. Robinson 1989. Corrosion 49, 710 716.

    [2]. K. Asami, K. Hashimoto 1979. Corros. Sci. 19, 1007 1017.

    [3]. T. von Moltke, P.C. Pistorius, R.F. Sandenbergh 1992. First In. Chromium Steel &

    alloys

    Congress, INFACON 6, vol.2, Chromium Steel and Alloy 185 195.

    [4]. P.K. Rastogi, B.K. Shah, A.K. Sinha, P.G. Kulkarni 1994. Brit. Corros. J. Vol. 29 78

    80.

    [5]. S. Azuma, H. Miyuki. J. Murayama. T. Kudo 1990. Corros. Eng. 667 676.

    [6]. R.F.A. Pettersson, J. Flyg. 2005. Influence of weld oxides on the corrosion of 316Lstainless

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    [7]. G. Berz, G.K. Wehner, L. Toth, A. Joshi 1974. J. Appl. Phys. 45 5312 -5316.

    [8]. WTIA, Chapter 4: Types of corrosion attack, WTIA/ACA technical note no. 13,

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    [9]. M. Keijzer 2004. Welding: to pickle or not pickle: no doubt about it. Published by: KCI

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    B. V.

    [10]. G.E. Coates 1990. Mater. Perform Vol. 29 61 -65.

    [11]. A.H. Tuthill, R. Avery 1992. Adv. Mater. Process Vol. 142 34 -38.

    [12]. American Welding Society Standards AWS D18.1/D18.1M:2009 .Specification for

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    of Austenitic Stainless Steel Tube and Pipe Systems in Sanitary (Hygienic) Applications.

    [13]. American Welding Society Standards AWS D18.2:2009, Guide To

    Weld Discoloration

    Levels On Inside Of Austenitic Stainless Steel Tube.

    [14]. J.Vagn Hansen. Reference colour charts for purity of purging gas in stainless steel

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    Force Institute Report 94.34.

    [15]. WTIA, Chapter 7: Stainless steel selection for specific environments, WTIA/ACAtechnical

    note no. 13, Stainless steels for corrosive environments, 1998.

    [16]. WTIA, Chapter 8: Corrosion in specific industries, WTIA/ACA technical note no. 13,

    Stainless steels for corrosive environments, 1998.

    [17]. ASTM G 48 03 Standard test methods for pitting and crevice corrosion resistance of

    stainless steels and related alloys by use of ferric chloride solution