<?xml version="1.0" encoding="ISO-8859-1"?><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance">
<front>
<journal-meta>
<journal-id>0872-1904</journal-id>
<journal-title><![CDATA[Portugaliae Electrochimica Acta]]></journal-title>
<abbrev-journal-title><![CDATA[Port. Electrochim. Acta]]></abbrev-journal-title>
<issn>0872-1904</issn>
<publisher>
<publisher-name><![CDATA[Sociedade Portuguesa de Electroquímica]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S0872-19042010000300004</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Studies on Corrosion of Annealed and Aged 18 Ni 250 Grade Maraging Steel in Sulphuric Acid Medium]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Poornima]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Jagannatha]]></surname>
<given-names><![CDATA[Nayak]]></given-names>
</name>
<xref ref-type="aff" rid="A02"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Shetty]]></surname>
<given-names><![CDATA[A. Nityananda]]></given-names>
</name>
<xref ref-type="aff" rid="A03"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Department of Science and Humanities  ]]></institution>
<addr-line><![CDATA[Bangalore ]]></addr-line>
<country>India</country>
</aff>
<aff id="A02">
<institution><![CDATA[,National Institute of Technology Department of Metallurgy and Materials Engineering ]]></institution>
<addr-line><![CDATA[ Karnataka]]></addr-line>
<country>India</country>
</aff>
<aff id="A03">
<institution><![CDATA[,National Institute of Technology Department of Chemistry ]]></institution>
<addr-line><![CDATA[ Karnataka]]></addr-line>
<country>India</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>00</month>
<year>2010</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>00</month>
<year>2010</year>
</pub-date>
<volume>28</volume>
<numero>3</numero>
<fpage>173</fpage>
<lpage>188</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_arttext&amp;pid=S0872-19042010000300004&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_abstract&amp;pid=S0872-19042010000300004&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_pdf&amp;pid=S0872-19042010000300004&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[The corrosion behavior of aged and annealed sample of 18 Ni 250 grade maraging steel was investigated in varied conditions of concentration and temperature of sulphuric acid medium, using electrochemical techniques like Tafel polarization and electrochemical impedance spectroscopy (EIS). The results obtained from both the techniques are in good agreement. These results have shown increase in corrosion rate of aged specimen with increase in concentration and temperature of sulphuric acid. With increase in concentration of sulphuric acid from 0.025 M to 0.25 M the corrosion rate of annealed sample was found to increase, but there after in 0.5 M, 0.75 M and 1 M, the rate of corrosion decreases, indicating passivation of alloy surface at higher concentration of sulphuric acid. The corrosion rate of aged specimen was found to be higher than that of the annealed specimen. Similar observations are revealed by SEM images. The thermodynamic parameters like activation energy, enthalpy of activation and entropy of activation were calculated.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[maraging steel]]></kwd>
<kwd lng="en"><![CDATA[acidic solutions]]></kwd>
<kwd lng="en"><![CDATA[EIS]]></kwd>
<kwd lng="en"><![CDATA[polarization]]></kwd>
<kwd lng="en"><![CDATA[SEM]]></kwd>
<kwd lng="en"><![CDATA[hydrogen overpotential]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ <p><b>Studies on Corrosion of Annealed and Aged 18 Ni 250 Grade Maraging Steel in    Sulphuric Acid Medium</b></p>     <P>&nbsp;</P>     <p>T. Poornima,<sup>1</sup> Nayak Jagannatha,<sup>2</sup> A. Nityananda Shetty<sup>3</sup>,<a href="#a1">*</a><a name="topa1"></a></p>     <P>&nbsp;</P>     <p><sup>1</sup> Department of Science and Humanities, PESIT Bangalore-560085, India </p>     <p><sup>2</sup> Department of Metallurgy and Materials Engineering, National Institute of    Technology, Karnataka, Surathkal, Srinivasnagar &#8211; 575 025, Karnataka,    India </p>     <p><sup>3</sup> Department of Chemistry, National Institute of Technology, Karnataka, Surathkal,    Srinivasnagar-575 025, Karnataka, India.</p>     <P>&nbsp;</P>      <p>DOI: 10.4152/pea.201003173 </p>      <P>&nbsp;</P>      ]]></body>
<body><![CDATA[<p><b>Abstract</b></p>     <p>The corrosion behavior of aged and annealed sample of 18 Ni 250 grade maraging    steel was investigated in varied conditions of concentration and temperature    of sulphuric acid medium, using electrochemical techniques like Tafel polarization    and electrochemical impedance spectroscopy (EIS). The results obtained from    both the techniques are in good agreement. These results have shown increase    in corrosion rate of aged specimen with increase in concentration and temperature    of sulphuric acid. With increase in concentration of sulphuric acid from 0.025    M to 0.25 M the corrosion rate of annealed sample was found to increase, but    there after in 0.5 M, 0.75 M and 1 M, the rate of corrosion decreases, indicating    passivation of alloy surface at higher concentration of sulphuric acid. The    corrosion rate of aged specimen was found to be higher than that of the annealed    specimen. Similar observations are revealed by SEM images. The thermodynamic    parameters like activation energy, enthalpy of activation and entropy of activation    were calculated.</p>      <p><b>Keywords:</b> maraging steel, acidic solutions, EIS, polarization, SEM, hydrogen    overpotential.</p>      <P>&nbsp;</P>      <p><b>Introduction</b></p>     <p>Corrosion of structural elements is a major issue for any industry because    of the chemical environment of the chemical processing. Maraging steels are    a special class of ultra high strength steels that differ from conventional    ones in that they are hardened by a metallurgical reaction that does not involve    carbon. Instead, these steels are strengthened by the precipitation of intermettalic    compounds at temperatures of about 480 &ordm;C. Maraging steels have slightly    better corrosion resistance than tempered martensite alloy steels. In industrial    and marine atmospheres, the corrosion rates of maraging steel are about half    of those of conventional steels. In saline and acidic solutions, maraging steels    show somewhat better corrosion resistance. They derive high strength from age    hardening of low carbon, Fe-Ni martensitic matrix [<a href="#1">1</a><a name="top1"></a>-<a href="#2">2</a><a name="top2"></a>].    The characteristics of this grey and white steel are high ductility, formability,    corrosion resistance, high temperature strength and easy to fabricate, weld    and treat with heat, and maintain an invariable size even after heat treatment    [<a href="#3">3</a><a name="top3"></a>]. These steels have emerged as alternative    materials to conventional quenched and tempered steels for advanced technologies    such as aerospace, nuclear and gas turbine applications. They frequently come    in contact with acids during cleaning, pickling, descaling, acidizing, etc.    Sulphuric acid is one of the most aggressive acids for iron and its alloys,    and is often used as a picking acid for steel and its alloys. But very less    study appears to be done in the area of corrosion behavior and corrosion inhibition    of maraging steel. So it is intended to study the corrosion behavior of maraging    steel in sulphuric acid medium. </p>     <p>According to available literature, atmospheric exposure of 18 Ni maraging steel    leads to corrosion in a uniform manner and it becomes completely rust covered    [<a href="#4">4</a><a name="top4"></a>]. Pit depths tend to be shallower than    high strength steels [<a href="#5">5</a><a name="top5"></a>]. Bellanger et al.    [<a href="#6">6</a><a name="top6"></a>] have shown the effect of slightly acid    pH with or without chloride ion in radioactive water on the corrosion of maraging    steel, and reported that corrosion behavior of maraging steel at the corrosion    potential depends on pH and intermediates remaining on maraging steel surface    in the active region favoring the passivity. The effect of carbonate ions in    slightly alkaline medium on the corrosion of maraging steel was investigated    by Bellanger, which reveals that corrosion potential does not change with carbonate    ions at a constant pH [<a href="#7">7</a><a name="top7"></a>]. Heat treatment    affects the corrosion rate. Critical and passive current densities increase    as the structure is varied from fully annealed to fully aged [<a href="#8">8</a><a name="top8"></a>].    Maraging steels are found to be less susceptible to hydrogen embrittlement than    common high strength steels owing to significantly low diffusion of hydrogen    in them [<a href="#9">9</a><a name="top9"></a>]. Several technical papers covering    alloy design, material processing, thermo-mechanical treatments, welding, strengthening    mechanisms, etc., have been published [<a href="#10">10</a><a name="top10"></a>].    The stress corrosion cracking behavior and also hydrogen embrittlement in these    steels have been studied quite extensively. The present paper reports the results    of studies carried out on the corrosion of 18 Ni 250 grade maraging steel in    sulphuric acid medium.</p>       <p><b>Experimental </b></p>     <p><b><i>Material </i></b></p>     <p>The maraging steel samples (M 250 grade) in annealed and aged condition were    taken from plates which were subjected to solution annealing treatment at 1088    &plusmn; 5 K for 1 hour followed by air cooling. Percentage composition of 18    Ni 250 grade maraging steel samples in annealed and aged condition is given    in Table 1. Cylindrical test coupons were cut from the plate and sealed with    epoxy resin in such a way that the area exposed to the medium is 0.503 cm<sup>2</sup>.    These coupons were polished as per standard metallographic practice, subjected    to belt grinding, followed by polishing on emery papers, finally on polishing    wheel using legated alumina to obtain mirror finish, degreased with acetone,    washed with distilled water and dried before immersing in the medium.</p>     ]]></body>
<body><![CDATA[<p>&nbsp;</p>      <p><b>Table 1.</b> Composition of the specimen.</p>     <p><img src="/img/revistas/pea/v28n3/28n3a04t1.gif" width="437" height="174">  </p>     
<p>&nbsp; </p>     <p><b><i>Medium</i></b></p>      <p>Standard solutions of sulphuric acid having concentrations 0.025 M, 0.05 M,    0.25 M, 0.5 M, 0.75 M and 1 M, were prepared by diluting analar grade sulphuric    acid by using double distilled water. Experiments were carried out using calibrated    thermostat at temperatures 303 K, 308 K, 313 K, 318 K, 323 K (&plusmn;0.5 K),    and solution was not deaerated during the electrochemical testing.</p>      <p><b><i>Electrochemical measurements </i></b></p>     <p>Electrochemical measurements were carried out in a potenciostat/galvanostat    AUTOLAB model PGSTAT30 controlled by a PC through the general purpose electrochemical    system (GPES) and frequency response analyzer (FRA) software provided by AUTOLAB.    EIS and Tafel polarization measurements were carried out using a conventional    three electrode Pyrex glass cell with platinum counter electrode and saturated    calomel electrode (SCE) as reference electrode. All the values of potential    are therefore referred to the SCE. Finely polished annealed and aged maraging    steel specimens of 0.503 cm<sup>2</sup> surface area were exposed to corrosion medium of    sulphuric acid having the above mentioned concentrations at different temperatures.</p>     <p>The potentiodynamic current-potential curves were recorded by polarizing the    specimen to -250 mV cathodically and +250 mV anodically with respect to OCP    at the scan rate of 5 mV/s. Electrochemical impedance spectroscopy (EIS), which    gives early information about the electrochemical processes at the metal solution    interface, has been used in many reports on corrosion studies [<a href="#11">11-12</a><a name="top11"></a>].    The corrosion behavior of the specimen in annealed and aged condition was also    investigated by EIS technique. In EIS technique a small amplitude of an AC signal    of 10 mV and frequency from 100 kHz to 0.01 Hz were recorded and impedance data    were analyzed. The charge transfer resistance R<sub>t</sub> was obtained from    Nyquist plot. The value of R<sub>t</sub> is inversely proportional to the corrosion    rate [<a href="#13">13</a><a name="top13"></a>] and the R<sub>p</sub> values    obtained from Tafel polarization are compared with R<sub>t</sub> values obtained    from Nyquist&#8217;s plot for good agreement.</p>     <p>In all the above measurements, at least three similar results were considered    and their average values are reported.</p>     ]]></body>
<body><![CDATA[<p>The scanning electron microscope images were recorded to establish the interaction    of acid medium with the metal surface using JEOL JSM-6380LA analytical scanning    electron.</p>       <p><b>Results and discussions</b></p>     <p><b><i>Tafel polarization measurements </i></b></p>     <p>The corrosion behaviors of annealed and aged samples of maraging steel specimens    were investigated at the above mentioned concentrations of sulphuric acid at    different temperatures using Tafel polarization technique. The potentiodynamic    polarization parameters, including corrosion potential (E<sub>corr</sub>), corrosion current    (I<sub>corr</sub>), polarization resistance (R<sub>p</sub>), anodic and cathodic slopes (b<sub>a</sub> and b<sub>c</sub>),    and corrosion rate, obtained from the Tafel studies, are summarised in Tables    2 and 3 for annealed and aged samples, respectively. Fig. 1 and 2 represent    potentiodynamic polarization curves of annealed and aged maraging steel specimens    in sulphuric acid as a function of concentration of sulphuric acid at 303 K.</p>      <p><i>Effect of temperature</i></p>     <p>Temperature is an important parameter in studies on material corrosion. The    dependence of temperature on corrosion rate reveals valuable thermodynamic parameters    like energy of activation, enthalpy and entropy of activation for the corrosion    process. The corrosion rate in acid solutions increases exponentially with increase    in temperature, because the hydrogen evolution overpotential decreases with    increase in temperature [<a href="#14">14</a><a name="top14"></a>]. The corrosion    of steel normally proceeds via two partial reactions in acid solutions. The    partial anodic reaction involves the oxidation of metal and formation of soluble    Fe<sup>2+</sup> ions, while the partial cathodic reaction involves the evolution    of hydrogen gas. It is clear from the data presented in Tables 1 and 2 that    the corrosion rate of both annealed and aged specimens increases with increasing    in the temperature of sulphuric acid medium from 303 K to 323 K. This may be    attributed to the fact that the hydrogen evolution overpotential decreases with    increase in temperature that leads to increase in cathodic reaction rate [<a href="#15">15</a><a name="top15"></a>].    These results are in agreement with the observation reported by Jones that,    in open system, the corrosion rate of iron increases with temperature up to    353 K [<a href="#16">16</a><a name="top16"></a>]. For annealed samples, with    increase in temperature, corrosion potential (E<sub>corr</sub>) and anodic Tafel    slope (b<sub>a</sub>) values were not affected significantly; but a significant    change in values of cathodic Tafel slope (b<sub>c</sub>) was observed. This    may be due to the change in hydrogen overvoltage, which in turn affects the    cathodic polarization curve. This may be also due to the contribution from concentration    polarization [<a href="#17">17</a><a name="top17"></a>], which leads to deviation    of cathodic curve from Tafel behavior at lower cathodic potentials, since the    variation in b<sub>c</sub> is more prominent at lower concentrations of acid.    In aged specimen Tafel slopes remain approximately the same. This indicates    that increase in temperature does not change the mechanism of corrosion reaction.    The variation of corrosion rate with temperature was utilized to calculate the    thermodynamic parameters such as activation energy (E<sub>a</sub>), enthalpy    of activation (&Delta;H) and entropy of activation (&Delta;S). </p>     <p>&nbsp;</p>      <p><b><a href="/img/revistas/pea/v28n3/28n3a04t2.gif" target="_blank">Table 2</a>.</b> Results    of Tafel polarization and the electrochemical impedance studies for the annealed    specimen. </p>     
<p>&nbsp;</p>     <p><b><a href="/img/revistas/pea/v28n3/28n3a04t3.gif" target="_blank">Table 3</a>.</b> Results    of Tafel polarization and the electrochemical impedance studies for the aged    specimen.</p>     
]]></body>
<body><![CDATA[<p>&nbsp; </p>     <p><img src="/img/revistas/pea/v28n3/28n3a04f1.gif"> </p>     
<p><b>Figure 1.</b> Polarisation curves of annealed maraging steel specimens in    different concentrations of sulphuric acid at 303 K.</p>     <p>&nbsp;</p>     <p><img src="/img/revistas/pea/v28n3/28n3a04f2.gif"> </p>     
<p><b>Figure 2.</b> Polarisation curves of aged maraging steel specimens in different    concentrations of sulphuric acid at 303K.</p>     <p>&nbsp;</p>     <p>According to Arrhenius law equation [<a href="#18">18</a><a name="top18"></a>],</p>      <p>ln k = A - (E<sub>a</sub>/RT)&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;(1) </p>      <p>where k is the rate constant, A is Arrhenius constant which depends on the    metal type, E<sub>a</sub> is the activation energy of the corrosion process    , R is the universal gas constant and T is the absolute temperature. The plot    of ln(corrosion rate) vs. reciprocal of absolute temperature, 1/T, gives straight    line whose slope = -Ea/R, from which the value of activation energy is calculated.    The Arrhenius plots for the annealed and aged specimens are shown in Fig. 3    and Fig. 4, respectively. Thus calculated values of activation energy are given    in Table 4. Entropy and enthalpy of activation (&Delta;H and &Delta;S) were    calculated from transition state theory (equation 2) [<a href="#19">19</a><a name="top19"></a>]:</p>     ]]></body>
<body><![CDATA[<p>&nbsp;</p>      <p><img src="/img/revistas/pea/v28n3/28n3a04e1.gif"> </p> </p>     
<p>&nbsp; </p>     <p>where h is Plank&#8217;s constant, N is Avogadro&#8217;s number. A plot of    ln(corrosion rate/T) vs. 1/T gives straight line with slope = -&Delta;H/R and    intercept = ln(R/Nh) + &Delta;S/R (Fig. 5 and Fig. 6). The significance of these    parameters is explained under the effect of concentration.</p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f3.gif">      
<p><b>Figure 3.</b> Arrhenius plots for annealed specimen of maraging steel in    sulphuric acid.</p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f4.gif">      
<p><b>Figure 4.</b> Arrhenius plots for aged specimen of maraging steel in sulphuric    acid.</p>     <p>&nbsp;</p>      <p><b>Table 4.</b> Activation parameters of corrosion reaction of annealed and aged specimens    in sulphuric acid.</p>     ]]></body>
<body><![CDATA[<p><img src="/img/revistas/pea/v28n3/28n3a04t4.gif"> </p>     
<p>&nbsp; </p>     <p><i>Effect of concentration</i></p>     <p>As can be seen from Fig. 1 and Fig. 2 the corrosion potential is shifted in    the positive direction, when the concentration of sulphuric acid is increased.    The positive shift in the corrosion potential, E<sub>corr</sub>, with increase    in concentration of acid indicates that the anodic process is much more affected    than the cathodic process [<a href="#20">20</a><a name="top20"></a>]. This observation    is in accordance with Murralidharan et al. [<a href="#21">21</a><a name="top21"></a>],    who proposed dependence of E<sub>corr</sub> and I<sub>corr</sub> on solution    parameters. It is evident from Fig. 1 and Table 2 that in case of aged specimen    the corrosion rate increases with increase in concentration of sulphuric acid,    and maximum corrosion is observed in 1 M sulphuric acid. Whereas in case of    annealed specimen, as seen from Fig. 2 and Table 3, the corrosion rate increases    with increase in concentration of sulphuric acid from 0.025M to 0.25 M. But    on further increase in concentration of sulphuric acid from 0.5 M to 1 M, the    corrosion rate decreases. This may be due to the passivation of the alloy surface    at high concentrations of sulphuric acid. The shift in E<sub>corr</sub> towards    noble values may be an indication of passivation. As can be observed in Fig.    2, for annealed specimen, with the increase in anodic potential, the corrosion    current density initially increases exponentially and then becomes gradual.    Passivity refers to loss of chemical reactivity experienced by certain metals    and alloys under particular environmental conditions. The metals most susceptible    to this kind of behavior are iron, nickel, silicon, chromium, titanium and alloys    containing these metals [<a href="#22">22</a><a name="top22"></a>]. Although    literature is not available in terms of passivity of maraging steel in sulphuric    acid, many reports are available regarding the passivation of iron and its alloys    in sulphuric acid. According to a number of authors, anodic passivity of metals    results from the formation of oxide and hydroxide films in the reaction of metals    with water. In general, the formation of passive film may occur according to    solid state reaction mechanism [<a href="#23">23-25</a><a name="top23"></a>].</p>     <p>&nbsp;</p>      <p><img src="/img/revistas/pea/v28n3/28n3a04e2.gif"> </p>     
<p>&nbsp; </p>     <p>or precipitation reaction,</p>     <p>&nbsp;</p>     <p><img src="/img/revistas/pea/v28n3/28n3a04e3.gif"> </p>     
]]></body>
<body><![CDATA[<p>&nbsp; </p>     <p>According to Boguscaw et al., passivation of iron in sulphuric acid (1 M) solution    is a result of metal water reaction, which is evidenced by thin hydrated oxyhydroxide    layer as detected by XPS [<a href="#26">26</a><a name="top26"></a>]. El-Kot    et al. reported the formation of passivating film on iron electrode upon anodic    oxidation in sulphuric acid and also dependence of passivation on the concentration    of the acid [<a href="#27">27</a><a name="top27"></a>].</p>     <p>&nbsp;</p> <img src="/img/revistas/pea/v28n3/28n3a04f5.gif">      
<p><b>Figure 5.</b> ln(corrosion rate/T) vs. 1/T plot for annealed sample of maraging    steel in sulphuric acid.</p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f6.gif">      
<p><b>Figure 6.</b> Polarisation curve of annealed maraging steel specimen in    1 M sulphuric acid solution at 303 K.</p>     <p>&nbsp;</p>      <p>For annealed specimen, the anodic and cathodic Tafel slopes (b<sub>a</sub>    and b<sub>c</sub>) showed approximately a constant value at lower concentration    of sulphuric acid (0.025 M, 0.05 M and 0.25 M), indicating that the corrosion    mechanism remains the same in lower concentrations of acid [<a href="#20">20</a><a name="top20"></a>].    At higher concentrations of acid (0.5 M, 0.75 M and 1 M) also, b<sub>a</sub>    and b<sub>c</sub> values remained constant, but the values are different from    those obtained at lower concentrations. This indicates that the mechanism of    corrosion process is different at lower concentration levels and higher concentration    levels; and mechanism remaining the same within the concentration ranges mentioned    at both the levels. The values of cathodic Tafel slopes at higher concentration    ( b<sub>c</sub>, 120 mV/dec) suggest that the hydrogen evolution reaction (HER)    is independent of sulphate ion concentration, the rate determining step in the    HER is the discharge reaction, a result which agrees with previous works [<a href="#17">17</a><a name="top17"></a>,<a href="#28">28-29</a><a name="top28"></a>].</p>     <p>&nbsp;</p>      <p><img src="/img/revistas/pea/v28n3/28n3a04e4.gif"> </p>     
]]></body>
<body><![CDATA[<p>&nbsp; </p>     <p>On the other hand, lower b<sub>a</sub> values are in accordance with Bockris    mechanism [<a href="#29">29</a><a name="top29"></a>] of dissolution/deposition    of iron, reproduced below. </p>     <p>&nbsp;</p>      <p><img src="/img/revistas/pea/v28n3/28n3a04e5.gif"> </p>     
<p>&nbsp; </p>     <p>The activation parameters for the corrosion process are listed in Table 4.    These values indicate that the energy of activation for corrosion process is    higher for annealed samples than for aged samples, in confirmation with the    difference in their corrosion rates, as discussed in the earlier section. A    very high value of activation energy obtained for annealed specimen at higher    concentration of acid may be an evidence for passivation of alloy surface at    higher concentrations of sulphuric acid. The entropy of activation for the corrosion    process, calculated from transition state theory equation, is found to be highly    negative in both the cases of annealed and aged samples. This implies that the    activated complex in the rate determining step represents association rather    than dissociation, indicating that a decrease in disorder takes place, on going    from reactant to the activated complex [<a href="#19">19</a><a name="top19"></a>].  </p>     <p>From the results of Tafel polarization we can observe that the corrosion rate    of annealed specimen is less when compared with aged specimen in sulphuric acid    medium. This may be attributed due to the fact that annealed specimens are solution    treated and air cooled. Annealed specimens contain entirely martensitic matrix    which is composed of predominantly iron and nickel. Hence, corrosion behavior    of annealed samples is similar to that of iron and nickel in acid medium. Aging    results in precipitation of intermetallics. Since these intermetallics have    different composition, their electrochemical behavior is expected to be different    compared to matrix [<a href="#30">30</a><a name="top30"></a>]. Also, there will    be strain fields around these coherent precipitates as a result of lattice mismatch    between the precipitate and the matrix, due to the difference in the crystal    structure and lattice parameters. These strain fields in combination with the    galvanic effect due to the composition difference leads to the enhanced corrosion    of aged samples than the annealed samples.</p>      <p><b><i>Electrochemical impedance spectroscopy</i></b></p>     <p>The results of potentiodynamic polarization experiments were confirmed by impedance    measurements, since EIS is a powerful technique in studying corrosion mechanism.    In order to get more information about the corrosion behavior of annealed and    aged maraging steel specimens, EIS measurements were carried out in sulphuric    acid medium at different concentrations and temperatures and they are displayed    as Nyquist plots in the present study. The Nyquist plots obtained for annealed    samples of maraging steel specimens in various acid concentrations and temperatures    are as shown in Fig. 7 and Fig. 8, respectively. The present study shows depressed    capacitive loop at high frequency range (HF) followed by an inductive loop that    is observed in low frequency (LF) region. The impedance spectra for different    Nyquist plots were analysed by fitting the experimental data to the equivalent    circuit model, as given in Fig. 9, which has been used previously to model iron/acid    interface [<a href="#13">13</a><a name="top13"></a>]. The constant phase element    is introduced in the circuit instead of pure double layer capacitor to give    more accurate fit [<a href="#31">31</a><a name="top31"></a>]. </p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f7.gif">      
]]></body>
<body><![CDATA[<p><b>Figure 7.</b> Nyquist diagrams of annealed maraging steel at different temperatures    in 0.25 M sulphuric acid.</p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f8.gif">      
<p><b>Figure 8.</b> Nyquist diagrams of annealed maraging steel in different concentrations    of sulphuric acid at 303 K.</p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f9.gif">      
<p><b>Figure 9.</b> Equivalent circuit used to fit experimental EIS data for the    corrosion of maraging steel specimen in sulphuric acid.</p>     <p>&nbsp;</p>       <p>The HF capacitive loop R<sub>ct</sub>-CPE can be attributed to charge transfer    reaction. These are not perfect semicircles, because the Nyquist plots obtained    in the real system represent a general behavior where the double layer at the    metal solution interface does not behave as an ideal capacitor [<a href="#32">32-33</a><a name="top32" id="top32"></a>].    The LF inductive loop R<sub>L</sub>-L can be attributed to relaxation process    obtained by adsorbed sulphate ions and protons [<a href="#34">34-35</a><a name="top34"></a>].    The point of intersection between inductive loop and the real axis represents    (R<sub>s</sub> + R<sub>ct</sub>). R<sub>s</sub> represents solution resistance    due to the ohmic resistances of corrosion product films and the solution enclosed    between the working electrode and the reference electrode. R<sub>ct</sub> represents    the charge transfer resistance whose value is a measure of electron transfer    across the surface and is inversely proportional to corrosion rate [<a href="#36">36</a><a name="top36"></a>].    The corrosion current density I<sub>corr</sub> can be calculated using charge    transfer resistance R<sub>ct</sub>, together with Stern-Geary equation 4 [<a href="#20">20</a><a name="top20"></a>].  </p>     <p>&nbsp;</p>      <p><img src="/img/revistas/pea/v28n3/28n3a04e6.gif"> </p>     
<p>&nbsp; </p>     ]]></body>
<body><![CDATA[<p>where A is the area of cross section of material under observation.</p>     <p>The value of R<sub>ct</sub> is inversely proportional to corrosion rate. Hence, EIS results    agree with the results obtained from Tafel polarization. The R<sub>ct</sub> values obtained    from Nyquist plot are in good agreement with R<sub>p</sub> values obtained from Tafel polarization.</p>       <p><b><i>Scanning electron microscope studies (SEM)</i></b></p>     <p>The SEM images of freshly polished surface of annealed and aged specimens of    maraging steel are given in Fig. 10(a) and Fig. 11(a) which show uncorroded    surface with few scratches due to polishing. The surface morphology of the annealed    and aged samples was examined by SEM immediately after corrosion tests in sulphuric    acid medium. The SEM images of corroded annealed samples in Fig. 10(b) show    degradation of the alloy. In the case of aged samples this degradation is highly    pronounced, as shown in Fig. 11(b). In both type of alloys the attack by sulphuric    acid is more at grain boundary since these regions are highly susceptible to    corrosion. In aged samples the intermetallic precipitation at grain boundary    may be responsible for higher rate of corrosion when compared to annealed samples.  </p>     <p>&nbsp; </p>  <img src="/img/revistas/pea/v28n3/28n3a04f10.gif">      
<p><b>Figure 10.</b> SEM images of annealed maraging steel specimen. (a. Freshly    polished surface. b. After immersion in sulphuric acid).</p>     <p>&nbsp;</p>  <img src="/img/revistas/pea/v28n3/28n3a04f11.gif">      
<p><b>Figure 11.</b> SEM images of aged maraging steel specimen. (a. Freshly polished    surface. b. After immersion in sulphuric acid).</p>     <p>&nbsp;</p>       <p><b>Conclusions</b></p>     ]]></body>
<body><![CDATA[<p>Based on the results of this investigation, the following conclusions may be    drawn.</p>     <p>1. The corrosion rate of both annealed and aged specimens is influenced by    temperature and concentration of sulphuric acid medium.</p>     <p>2. The corrosion rate of aged specimens under investigation increases with    increase in concentration and temperature of sulphuric acid medium.</p>     <p>3. The corrosion rate of annealed specimen increases with increase in concentration    of sulphuric acid medium up to 0.25 M, but at 0.5 M and above, passivation of    alloy surface may be responsible for decrease in corrosion rate. With increase    in temperature corrosion rate increases. </p>     <p>4. The corrosion kinetics follows Arrhenius law.</p>     <p>5. The corrosion rate of aged sample is higher when compared with the annealed    specimen in sulphuric acid medium due to galvanic effect and strain fields.</p>     <P>&nbsp;</P>     <p><b>References </b></p>     <!-- ref --><p><a href="#top1">1</a><a name="1"></a>. K.Y .Sastry, R. Narayanan, C.R Shamantha,    S.S Sunderason, S.K. Seshadri, V.M. Radhakrishnan, K.J.L. Iyer and S. Sundararajan,    <i>Mater. Sci. Technol.</i> 19 (2003) 375. [10.1179/026708303225010632]&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000121&pid=S0872-1904201000030000400001&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --><p><a href="#top2">2</a><a name="2"></a>. ASM Handbook, vol.1,10th ed, 1990, 796.</p>     ]]></body>
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<ref-list>
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<nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sastry]]></surname>
<given-names><![CDATA[K.Y .]]></given-names>
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<surname><![CDATA[Narayanan]]></surname>
<given-names><![CDATA[R.]]></given-names>
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<surname><![CDATA[Shamantha]]></surname>
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<surname><![CDATA[Seshadri]]></surname>
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</article>
