<?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>S0872-19042012000600005</article-id>
<article-id pub-id-type="doi">10.4152/pea.201206419</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Corrosion Inhibition of Aluminum in Aqueous Alkaline Solutions by Alginate and Pectate Water-Soluble Natural Polymer Anionic Polyelectrolytes]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Zaafarany]]></surname>
<given-names><![CDATA[I.]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Umm Al-qura University Faculty of Appl. Sci. Chem. Dept]]></institution>
<addr-line><![CDATA[Makkah Al-Mukaramha ]]></addr-line>
<country>Saudi Arabia</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>11</month>
<year>2012</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>11</month>
<year>2012</year>
</pub-date>
<volume>30</volume>
<numero>6</numero>
<fpage>419</fpage>
<lpage>426</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_arttext&amp;pid=S0872-19042012000600005&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_abstract&amp;pid=S0872-19042012000600005&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_pdf&amp;pid=S0872-19042012000600005&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[The influence of water-soluble alginates (Alg) and pectates (Pect) anionic polyelectrolytes as natural polymers containing secondary alcoholic groups on the rate of dissolution of aluminum metal in alkaline medium has been investigated by gasometric and weight-loss techniques. The results showed that addition of alginates or pectates to the tested solutions leads to a remarkable decrease in the corrosion rate of Al in NaOH. The magnitude of inhibition efficiency was found to be larger in case of pectates. Factors affecting the corrosion process such as the concentration of the inhibitor and the corrosion medium, structure of the inhibitor and temperature have been examined. The kinetic parameters of corrosion have been evaluated and a suitable mechanism for the inhibition is discussed.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[corrosion]]></kwd>
<kwd lng="en"><![CDATA[inhibitors]]></kwd>
<kwd lng="en"><![CDATA[anionic]]></kwd>
<kwd lng="en"><![CDATA[polyelectrolytes]]></kwd>
<kwd lng="en"><![CDATA[aluminum]]></kwd>
<kwd lng="en"><![CDATA[kinetics]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ 

    <p><b>Corrosion Inhibition of Aluminum in Aqueous Alkaline Solutions by Alginate and Pectate Water-Soluble Natural Polymer Anionic Polyelectrolytes</b></p>

    <p><b>I. Zaafarany<sup><a href="#0">*<a/></sup></b></p>

    <p><i> Chem. Dept. Faculty of Appl. Sci., Umm Al-qura University, Makkah Al-Mukaramha, Saudi Arabia.</i></p>


<!--     <p>&nbsp;</p>
    <p>doi: 10.4152/pea.201206419</p> -->


    <p>&nbsp;</p>
    <p><b>Abstract</b></p>

    <p>The influence of water-soluble alginates (Alg) and pectates (Pect) anionic 
polyelectrolytes as natural polymers containing secondary alcoholic groups on the rate 
of dissolution of aluminum metal in alkaline medium has been investigated by 
gasometric and weight-loss techniques. The results showed that addition of alginates or 
pectates to the tested solutions leads to a remarkable decrease in the corrosion rate of Al 
in NaOH. The magnitude of inhibition efficiency was found to be larger in case of 
pectates. Factors affecting the corrosion process such as the concentration of the 
inhibitor and the corrosion medium, structure of the inhibitor and temperature have been 
examined. The kinetic parameters of corrosion have been evaluated and a suitable 
mechanism for the inhibition is discussed.</p>

    <p><b><i>Keywords:</i></b> corrosion, inhibitors, anionic, polyelectrolytes, aluminum, kinetics.</p>


    ]]></body>
<body><![CDATA[<p>&nbsp;</p>
    <p><b>Introduction</b></p>

    <p>The development of inhibitors for aluminum corrosion in aqueous solution, in 
particularly in alkaline media has attracted many investigators. However, the 
influence of inhibitors has been the subject of numerous investigators; the 
corrosion mechanisms as well as the role of inhibitors are not completely 
explained.</p>

    <p>Although many organic [1-7], inorganic [8,9] and synthesized polymeric [10,11] 
compounds were applied as inhibitors for reducing the aluminum corrosion in 
alkaline media, little attention has been focused for applying natural polymers as 
inhibitors [12]. Indeed, sulfated carrageenan [13,14] and carboxymethyl cellulose 
[15,16] as natural polymers as well as polyacrylic acid [17] as a synthetic 
polymer have been successfully used as inhibitors for corrosion of iron in acidic 
media.</p>

    <p>In view of the above aspects, the present work of using alginate and pectate 
polysaccharides as natural polymeric inhibitors for Al metal in NaOH has been 
undertaken with a view at shedding some lights on the mechanism of corrosion. 
In addition, it is of interest to extend our work carried out in our laboratory on 
natural polymers, particularly on polysaccharides, as a part of a series of 
investigations [18-23].</p>


    <p>&nbsp;</p>
    <p><b>Experimental</b></p>

    <p><b><i>Materials</i></b></p>

    <p>All materials used were of analytical grade. Doubly distilled water was used in 
all preparations. The temperature was controlled within &pm; 0.1 &deg;C. 
Sodium alginate and sodium pectate (Fluka) were used without further 
purification. Aluminum metal used was 99.98 purity (Ventron Corp, Japan). The 
degrees of substitution for alginates and pectates (apple) were found to be 3.84 
and 4.12 mol/g (0.7 and 0.64 mol/mol), respectively. Again, the inherent 
viscosities measured by using Ubbelhode viscometer were found to be 3.84 and 
0.8 dL/g for alginates and pectates, respectively.</p>


    <p><b><i>Preparation of alginate and pectate sols</i></b></p>

    ]]></body>
<body><![CDATA[<p>Alginate and pectate sols were prepared as described elsewhere [18-22]. This 
process was performed by stepwise addition of the powder reagent to bidistilled 
water whilst vigorously stirring the solutions to avoid the formation of lumpy 
precipitates, which swell with difficulty.</p>


    <p><b><i>Techniques of measurements</i></b></p>

    <p>The rates of corrosion were determined volumetrically. This process takes place 
by measuring the evolved hydrogen produced from dissolution of aluminum in 
NaOH. Rectangular specimen of metal aluminum of 3 cm long and 1.9 cm in 
diameter were used without further polishing to ensure reproducible surface. 
However, they were washed with carbon tetrachloride, absolute ethyl alcohol and 
then dried in acetone and stored in free desiccators prior to the use in corrosion 
testing. The specimens were suspended by means of a glass hook in the tested 
solutions of NaOH which were previously placed into a conical flask fitted with a 
graded side-arm burette filled with bidistilled water as described elsewhere 
[17,24, 25]. The conical flasks were thermostated in a controlled water-bath at 
the desired temperature within &pm;0.1 &deg;C. When the NaOH solution had attained 
the temperature of the thermostat, the Al specimen was immersed into the alkali 
solution. The course of reaction was followed gasometrically by recording the 
volume of evolved hydrogen as a function of time.</p>

    <p>Some kinetic measurements were performed using the classical weight-loss 
method [25] in order to check the reproducibility of the gasometric data obtained. 
The analyses of the results obtained were found to be in a good agreement with 
each other within the experimental errors (&pm;4%). This fact may indicate the 
reproducibility of the results obtained, gasometrically.</p>

    <p>All experiments were repeated using different concentrations of NaOH and 
inhibitors at various temperatures. The results used were at least an average of 
five experimental runs. No stirring of the corrosion medium was employed.</p>


    <p>&nbsp;</p>
    <p><b>Results</b></p>

    <p>The volume of the evolved hydrogen (or the loss in weight of Al metal) as a 
function of time may be taken as the rate of dissolution of aluminum in sodium 
hydroxide as is illustrated by Eqs. (<a href="#e1">1</a>) and (<a href="#e2">2</a>), respectively,</p>

    <p>&nbsp;</p>
<a name="e1">
<img src="/img/revistas/pea/v30n6/30n6a05e1.jpg">
    
<p>&nbsp;</p>
<a name="e2">
<img src="/img/revistas/pea/v30n6/30n6a05e2.jpg">
    
]]></body>
<body><![CDATA[<p>&nbsp;</p>

    <p>where R<sub>c</sub> is the rate of corrosion, S is the surface area of Al metal (cm<sup>2</sup>), t is the 
time (min), V<sub>H</sub> is the volume of evolved hydrogen (mL) and &Delta;W is the loss in 
mass (mg) of Al metal into the corrosive medium.</p>

    <p>Typical plots are shown in Figs. <a href="#f1">1</a> and <a href="#f2">2</a>, respectively.</p>

    <p>&nbsp;</p>
<a name="f1">
<img src="/img/revistas/pea/v30n6/30n6a05f1.jpg">
    
<p>&nbsp;</p>
<a name="f2">
<img src="/img/revistas/pea/v30n6/30n6a05f2.jpg">
    
<p>&nbsp;</p>

    <p>The rate of corrosion can 
be obtained from the slopes of such plots. The values of R<sub>c</sub> were calculated by 
using the method of least-square and are summarized in <a href="#t1">Table 1</a>.</p>

    <p>&nbsp;</p>
<a name="t1">
<img src="/img/revistas/pea/v30n6/30n6a05t1.jpg">
    
<p>&nbsp;</p>

    <p>The percentage inhibition efficiency (I.E %) of the selected alginate and pectate 
polysaccharides as natural polymeric inhibitors was calculated using the 
following equation</p>

    ]]></body>
<body><![CDATA[<p>&nbsp;</p>
<a name="e3">
<img src="/img/revistas/pea/v30n6/30n6a05e3.jpg">
    
<p>&nbsp;</p>

    <p>where R<sub>c</sub><sup>o</sup> and R<sub>c</sub><sup>'</sup> are the corrosion rates of Al metal in the absence and presence
of natural polymeric inhibitors, respectively. 


    <p>&nbsp;</p>
    <p><b>Discussion</b></p>

    <p>It is well known that increasing the [OH<sup>-</sup>] will increase the activity of OH<sup>-</sup> [26] 
and, hence, should increase the dissolution of Al metal as was experimentally 
observed. The observed fractional-order for [OH<sup>-</sup>]-dependence of the corrosion 
rates means that at least one of the corrosion paths of Al metal in NaOH should 
involve hydroxide ion in the rate-determining step.</p>

    <p>On the other hand, it was observed that the addition of either alginate or pectate 
sol to the tested solutions of Al metal in NaOH is accompanied by a remarkable 
decrease in the corrosion rate of aluminum.</p>

    <p>In view of the above interpretations and the experimental observations, a suitable 
mechanism for corrosion may be suggested. It involves the electrochemical 
process [27] resulting from dissolution of Al metal in the alkali. This process can 
be expressed by anodic and cathodic processes, Eqs. (<a href="#e4">4</a>) and (<a href="#e5">5</a>), respectively:</p>

    <p>&nbsp;</p>
<a name="e4">
<img src="/img/revistas/pea/v30n6/30n6a05e4.jpg">
    
<p>&nbsp;</p>
<a name="e5">
<img src="/img/revistas/pea/v30n6/30n6a05e5.jpg">
    
]]></body>
<body><![CDATA[<p>&nbsp;</p>

    <p>The overall electroochemical process is</p>

    <p>&nbsp;</p>
<a name="e6">
<img src="/img/revistas/pea/v30n6/30n6a05e6.jpg">
    
<p>&nbsp;</p>

    <p>Alginates and pectates are water-soluble polysaccharides of linear block 
copolymer structures consisting of D-mannuronic and L-gulurunic acid units 
linked through &beta;(1 &rarr; 4) positions [28]. The principal structural difference 
between them is the position of the two C-2 and C-3 hydroxyl groups being cis-
position in alginates and trans-position in pectates, respectively. When the 
conformation is considered, axial-equatorial and equatorial-equatorial exist. 
These natural polymers are anionic in nature owing to the presence of 
carboxylate groups. The carboxylate groups probably being equatorial in both 
[29]. These polysaccharides are assumed to be deprotonated in alkaline solutions 
to give the corresponding reactive alkoxides [18,20] as follows:</p>

    <p>&nbsp;</p>
<a name="e7">
<img src="/img/revistas/pea/v30n6/30n6a05e7.jpg">
    
<p>&nbsp;</p>
<a name="e8">
<img src="/img/revistas/pea/v30n6/30n6a05e8.jpg">
    
<p>&nbsp;</p>

    <p>It has been reported [30] that the inhibitor can affect the corrosion rate of metals 
in the corrosive media if it is able to affect the kinetics of dissolution or alter the 
position of electrochemical behaviour. This effect takes place when a thin film of 
an inhibitor is formed on the surface of the metal by either the interaction or 
adsorption processes. The protective film will isolate the metal from the 
corrosive medium, i.e. it decreases the corrosion rate. Under the influence of 
highly negative potentials such as in case of Al metal in alkaline solutions [3035], 
all anionic organic compounds are expelled by the electric double layer and, 
hence, cannot affect the corrosion rate significantly. On the other hand, the 
cationic material strongly inhibits the corrosion processes owing to its adsorption 
on the metal surface.</p>

    <p>As shown in <a href="#t1">Table 1</a>, addition of small amounts of alginates or pectates as 
anionic polyelectrolytes to Al in NaOH leads to a remarkable inhibition of the 
corrosion rates of aluminum metal. This result may be explained by the 
adsorption of negative alkoxides formed by the deprotonation processes or the 
anionic polymer itself on the positive sites which may be formed as a result of 
electrons liberation in the anodic processes. The net result of adsorption is the 
formation of an inhibitor thin film on the aluminum surface. The formed film 
will prevent more Al atoms from leaving the metal surface to dissolve in the 
corrosive medium. This means that the corrosion rate is decreased. Therefore, the 
anodic reaction may be suggested to be the rate-determining step in the present 
corrosion process. Again, the presence of lone pairs of electrons on the oxygen 
atoms of the hydroxyl groups may enhance the interaction between the inhibitors 
and the positive sites formed on Al surface. Moreover, Khairou and El-Sayed 
[36] reported that the functional hydroxyl groups of the natural-polymer anionic 
polyelectrolytes could form bridges between the polymer and the metal surface 
and, hence, affecting the inhibition behavior.</p>

    ]]></body>
<body><![CDATA[<p>The inhibition efficiency (% I.E) was found to increase with increasing the 
concentration of the added inhibitors as shown in <a href="#t2">Table 2</a>.</p>

    <p>&nbsp;</p>
<a name="t2">
<img src="/img/revistas/pea/v30n6/30n6a05t2.jpg">
    
<p>&nbsp;</p>

    <p>The magnitude of the I.E was found to be larger in case of pectates rather than in alginates. The 
inhibition efficiency may be affected by many factors such as the adsorption of 
the additives on Al metal surface which depend on some physicochemical 
properties, e.g., the functional groups, steric factors and electronic and 
geometrical configurations of the inhibitor [13,14]. The geometrical structure of 
the hydroxyl groups in C-2 and C-3 may play an important role in this behavior. 
The presence of OH groups in cis-position in alginates tends to decrease the 
ability of adsorption of the inhibitors on Al metal surface owing to the hindrance 
effect, compared with that in case of pectates where the OH groups exist in the 
trans-position. Here, the hindrance effect is relatively small. This may explain the 
small inhibition effects of alginates compared to that of pectates.</p>

    <p>The orders with respect to the alginate and pectate inhibitors concentrations (log 
[Inhibitor] vs. log Rc) were found to be 1.4 &pm; 0.1 and 1.2 &pm; 0.1, respectively. The 
magnitude of this order may also reflect the efficiency of the inhibitor on the 
corrosion rate. In addition, the fractional order observed with respect to alginate 
and pectate concentrations may indicate the formation of intermediates through 
the adsorption process. Furthermore, the kinetic parameters of the corrosion 
inhibition were calculated from the dependence of the corrosion rate on the 
temperature. This dependence was found to fit the Arrhenius and Eyring 
relationships [37], which required that plots of 1/T vs. ln R<sub>c</sub> or 1/T vs. ln 
(hR<sub>c</sub>/RT) for Arrhenius and Eyring equations, respectively, to be linear with 
positive intercepts on Y axes as was experimentally observed. The kinetic 
parameters can be evaluated from the slopes and intercepts of such plots. The 
values of the kinetic parameters were calculated using the least-square method 
and are summarized along with that of poly(vinyl alcohol) as synthetic polymers 
[38] in <a href="#t3">Table 3</a>.</p>

    <p>&nbsp;</p>
<a name="t3">
<img src="/img/revistas/pea/v30n6/30n6a05t3.jpg">
    
<p>&nbsp;</p>

    <p>The positive values of &Delta;H<sup>#</sup> reflect the endothermic process of 
adsorption of the inhibitors on Al surface. The negative values of &Delta;S<sup>#</sup> may reflect 
the association mechanism of corrosion, i.e., the decrease in disorderly takes 
place on going from reactants to the activated states [13].</p>

    <p>It is also noticed that addition of small amounts of the inhibitor to the tested 
solutions alters the values of &Delta;S<sup>#</sup> (in absence of inhibitors) to a less negative one, 
i.e., inhibits the corrosion rates. This result may be considered as an indirect 
evidence to support the proposed mechanism.</p>


    <p>&nbsp;</p>
    ]]></body>
<body><![CDATA[<p><b>Conclusion</b></p>

    <p>1. We have proved (<a href="#t1">Table 1</a> and <a href="#f1">Fig. 1</a>) that alginate and pectate anionic 
polyelectrolytes as natural polymers are effective inhibitors for corrosion of 
aluminum in alkaline medium.</p>

    <p>2. Pectates are more active for corrosion inhibition than alginates. This may be 
due to the geometrical configuration of the functional groups of the inhibitors, 
which play an important role in the magnitude of inhibition efficiency.</p>

    <p>3. We would believe that natural or synthetic polymers containing the same 
functional groups will have the same corrosion behavior and, hence, may 
proceed through similar corrosion mechanism.</p>


    <p>&nbsp;</p>
    <p><b>References</b></p>

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    <p>&nbsp;</p>
    <p><a name=0></a><sup><a href="#top">*</a></sup>Corresponding author. E-mail address: <a href="mailto:ishaq_zaafarany@yahoo.com">ishaq_zaafarany@yahoo.com</a></p>

    <p>Received 13 January 2013; accepted 13 February 2013</p>

    <p><a href="http://www.peacta.org" target="_blank">www.peacta.org</a> </p>


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