<?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>S0872-19042015000100006</article-id>
<article-id pub-id-type="doi">10.4152/pea.201501049</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Effect of Process Parameters on Corrosion Resistance of Ni-P-Al2O3 Composite Coatings Using Electrochemical Impedance Spectroscopy]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Gadhari]]></surname>
<given-names><![CDATA[Prasanna]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Sahoo]]></surname>
<given-names><![CDATA[Prasanta]]></given-names>
</name>
<xref ref-type="aff" rid="A01"/>
</contrib>
</contrib-group>
<aff id="A01">
<institution><![CDATA[,Jadavpur University Department of Mechanical Engineering ]]></institution>
<addr-line><![CDATA[Kolkata ]]></addr-line>
<country>India</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>01</month>
<year>2015</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>01</month>
<year>2015</year>
</pub-date>
<volume>33</volume>
<numero>1</numero>
<fpage>49</fpage>
<lpage>68</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_arttext&amp;pid=S0872-19042015000100006&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_abstract&amp;pid=S0872-19042015000100006&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://scielo.pt/scielo.php?script=sci_pdf&amp;pid=S0872-19042015000100006&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Electroless nickel composite coatings are developed by incorporating soft/hard particles into Ni-P coatings, to improve mechanical as well as tribological properties. The objective of the present work is to investigate the effect of various coating process parameters on the corrosion behavior of Ni-P-Al2O3 composite coating deposited on mild steel substrate. The electrochemical impedance spectroscopy test is used to evaluate the corrosion behavior of the heat treated composite coatings at various annealing temperatures (300 °C, 400 °C, and 500 °C). Corrosion properties, charge transfer resistance (Rct) and double layer capacitance (Cdl), are optimized using Taguchi based grey relational analysis to improve the corrosion resistance of the coating. Concentration of nickel source, concentration of reducing agent, concentration of alumina particles and annealing temperature, are considered as a main design factor for optimization of electrochemical properties. Analysis of variance (ANOVA) is used to find out the optimum combination of coating process parameters. From ANOVA result, it is found that the concentration of Al2O3 particles and annealing temperature have significant influence on the corrosion resistance of the composite coatings. Concentration of reducing agent has moderate influence on the corrosion resistance. Surface morphology of the coated surface is studied using SEM (scanning electron microscopy) and chemical composition of the coating is studied using EDX (energy dispersive X-ray analysis). The XRD (X-ray diffraction analysis) is used to understand the phase transformation behavior of the composite coatings.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[Ni-P-Al2O3 composite coating]]></kwd>
<kwd lng="en"><![CDATA[corrosion]]></kwd>
<kwd lng="en"><![CDATA[electrochemical impedance spectroscopy]]></kwd>
<kwd lng="en"><![CDATA[optimization]]></kwd>
</kwd-group>
</article-meta>
</front><body><![CDATA[ 

<!--     <p>&nbsp;</p>
    <p>doi: 10.4152/pea.201501049</p> -->

    <p><b>Effect of Process Parameters on Corrosion Resistance of Ni-P-Al<sub>2</sub>O<sub>3</sub> Composite Coatings Using Electrochemical Impedance Spectroscopy</b></p>

    <p>
<b>Prasanna Gadhari</b><sup></sup>
 and <b>Prasanta Sahoo</b><sup><a href="#0">*</a></sup>
</p>

    <p><i>Department of Mechanical Engineering, Jadavpur University, Kolkata, 700032, India</i></p>


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

    <p>Electroless nickel composite coatings are developed by incorporating soft/hard particles 
into Ni-P coatings, to improve mechanical as well as tribological properties. The 
objective of the present work is to investigate the effect of various coating process 
parameters on the corrosion behavior of Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating deposited on 
mild steel substrate. The electrochemical impedance spectroscopy test is used to 
evaluate the corrosion behavior of the heat treated composite coatings at various 
annealing temperatures (300 &deg;C, 400 &deg;C, and 500 &deg;C). Corrosion properties, charge 
transfer resistance (R<sub>ct</sub>) and double layer capacitance (C<sub>dl</sub>), are optimized using Taguchi 
based grey relational analysis to improve the corrosion resistance of the coating. 
Concentration of nickel source, concentration of reducing agent, concentration of 
alumina particles and annealing temperature, are considered as a main design factor for 
optimization of electrochemical properties. Analysis of variance (ANOVA) is used to 
find out the optimum combination of coating process parameters. From ANOVA result, 
it is found that the concentration of Al<sub>2</sub>O<sub>3</sub> particles and annealing temperature have 
significant influence on the corrosion resistance of the composite coatings. 
Concentration of reducing agent has moderate influence on the corrosion resistance. 
Surface morphology of the coated surface is studied using SEM (scanning electron 
microscopy) and chemical composition of the coating is studied using EDX (energy 
dispersive X-ray analysis). The XRD (X-ray diffraction analysis) is used to understand 
the phase transformation behavior of the composite coatings.</p>

    <p><b><i>Keywords:</i></b> Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating, corrosion, electrochemical impedance 
spectroscopy, optimization.</p>


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

    <p>Electroless nickel coatings are not only used for environmental protection of base 
metal but also to protect it from corrosion and wear. Most machine parts, tools 
and equipments in the industries are affected due to environmental changes, 
corrosion, erosion, wear and friction. It is essential to protect the machine tools, 
equipments and materials from corrosion, wear and erosion. It may be achieved 
by applying specific coatings on the base material to protect them from corrosion 
and environmental changes and also to increase hardness, wear and friction 
resistance. Ni-P electroless plating is one of the most important surface-
engineering technology, which is applied in industrial fields. Composite coatings 
are more popular in various industries like as mechanical, chemical, automobile, 
textile, aerospace, etc., due to excellent mechanical and tribological properties 
[1]. Electroless nickel plating is a metal deposition process involving chemical 
reaction. It is an auto-catalytic chemical technique used to deposit layers of 
nickel and phosphorus on ferrous or non-ferrous solid substrates. This process 
relies on the presence of a reducing agent, which reacts with metallic ions to 
deposit metal. When the substrate is dipped in the electroless bath, it develops 
potential. Due to this, negative and positive ions are attracted towards the surface 
of the substrate and release the energy by charge transfer process. Electroless 
bath consists of source of metallic ions, source of reducing agent, complexing 
agent, wetting agent, stabilizer, and pH controlling agent. The electroless Ni-P 
coatings containing more than 7% phosphorus have an excellent corrosion 
resistance. Therefore, these coatings are used in industries which have corrosive 
environments such as in mining, chemical, textile, oil and gas, etc. In general, 
electroless coating is divided into four group viz., pure nickel coatings, alloy and 
poly alloy coatings, composite coatings, and nano coatings [2]. These coatings 
have uniform thickness across all the surfaces irrespective of complex geometry 
and sharp edges.</p>

    <p>Incorporation of fine inert (soft/hard) particles into electroless nickel coatings 
yields electroless nickel composite coatings. In composite coatings, second phase 
particles are deposited on the surface of the substrate and are well embedded in 
the Ni-P matrix during the deposition process. To improve corrosion resistance, 
lubricity and to reduce friction, soft particles like as PTFE. MoS<sub>2</sub>, HBN, and 
graphite are introduced in the electroless Ni-P coatings. On the other hand, hard 
particles like as SiC, WC, Al<sub>2</sub>O<sub>3</sub>, Si<sub>3</sub>N<sub>4</sub>, 
CeO<sub>2</sub>, TiO<sub>2</sub>, ZrO<sub>2</sub>, and diamond, etc., are 
incorporated in the electroless Ni-P coatings to increase hardness, wear 
resistance, corrosion resistance, and frictional resistance [3]. To get excellent 
properties, the second phase particles must be uniformly distributed during the 
deposition process otherwise, due to non-uniform distribution of particles, 
numerous defects are formed because of segregation and agglomeration of 
composite or nano particles with high surface energy and activity in the 
electroless bath [4]. The tribological and mechanical properties of composite 
coatings are significantly improved with appropriate heat treatment at and above 
400 &deg;C for one hour [5]. Various hard particles like, SiC, TiC, TiB<sub>2</sub>, B4C 
particles are normally used as reinforcement phase. Out of these particles Al<sub>2</sub>O<sub>3</sub> 
is widely used because of its high elastic modulus, strength retention at high 
temperature, and high wear resistance [6]. Usually, the presence or availability of 
composite particles in the electroless Ni-P composite coatings depends on 
incorporation of particles on the coating surface and holding time of the particle 
on the coating surface [7]. Deposition rate, incorporation rate of the composite 
particles, roughness and hardness of the composite coating depend on the 
concentration of alumina particles in the elecroless bath [8]. Corrosion resistance 
of electroless Ni-P coatings is higher than chromium alloy and pure nickel. In a 
particular environment higher corrosion resistance is due to amorphous nature 
and the passivity of the Ni-P coating [9]. Various factors such as phosphorus 
content, porosity of the coating and heat treatment of the coating significantly 
affect the corrosion resistance of the composite coating. The porosity of the 
composite coating is increased with increase in the surface roughness. Roughness 
of the coating depends on the mechanical preparation of the surface of the 
substrate and deposition of the second phase particles on the coated surface of the 
sample. The porous composite coatings have lower corrosion resistance as 
compared to non-porous composite coatings. Hence, to avoid the porosity of the 
coating, the second phase particles must be uniformly distributed over the coated 
surface of the sample. Wetting agents play important role in the deposition of the 
composite coating. In the presence of wetting agent, the second phase particles 
get uniformly distributed over the coated surface and it also improves the 
corrosion resistance of the composite coating. Recently, much attention is being 
paid on composite coatings due to their excellent performance, instead of Ni-P 
and Ni-B coatings [4].</p>

    <p>Abdel Salam Hamdy et al. [10] have observed the improvement in corrosion 
resistance (100 times) of the coatings, in the presence of alumina particles as 
compared to steel substrate. The surface resistance of Ni-P coating is 
0.78 &times; 10<sup>4</sup> &Omega; cm<sup>2</sup> and for composite coatings it is 
7.00 &times; 10<sup>4</sup> &Omega;cm<sup>2</sup>. Bigdeli and 
Allahkaram [11] have found increase in corrosion resistance (Rc) with decrease in 
the constant phase elements (CPE) of the Ni-P and Ni-P-SiC composite 
coatings. The Ni-P-SiC composite coating has higher corrosion resistance as 
compared to Ni-P coating, due to reduction in effective metallic area for 
corrosion. Zarebidaki et al. [12] have confirmed that the corrosion resistance of 
Ni-P-SiC coating depends on the dispersion of nano particles throughout the 
coating. At higher concentration, SiC particles are agglomerated on the coated 
surface, which provokes the porosity of the composite coating. On the basis of 
Nyquist plot, it is confirmed that Ni-P coatings have better corrosion resistance 
as compared to Ni-P/nano-SiC composite coatings. The porosity of the 
composite coatings is decreased with increase in incorporation of alumina 
particles in the composite coatings, which improves the corrosion resistance of 
the coating. Whereas Stankiewicz et al. [13] have observed that the addition of 
zirconium oxide in Ni-P and Ni-P-W coatings adversely affect corrosion 
resistance after 1 hour immersion in 3.5% NaCl medium, Allahkaram et al. [14] 
have found that addition of nano-particles in Ni-P coating reduces the effective 
metal area, which is prone to corrosion. The charge transfer resistance (R<sub>ct</sub>) of a 
nano composite coating is higher than that of Ni-P coating, meaning that the 
composite coating has higher corrosion resistance than the electroless nickel 
coating. The corrosion resistance of EN silicon carbide composite coatings 
depends on the spreading of nano particles throughout the coatings. Parveen et al. 
[15] have found the improvement in corrosion resistance of zinc coating in the 
presence of carbon nanotube particles.</p>

    <p>The corrosion resistance of a coating depends on various factors such as 
phosphorus content, type of corrosion solution and incorporation of second phase 
particles in Ni-P coatings. Zarebidaki et al. [16] have observed that the proper 
heat treatment of the coating significantly improves the coating density and 
structure. The experimental results show that the Ni-P-CNT composite coating 
has better corrosion resistance as compared to Ni-P coating. Corrosion resistance 
of the Ni-P coating is reduced due to increase in effective metallic area. Lee [17] 
has performed immersion tests in 3.5 wt.% NaCl solution for different test 
durations (one hour to 720 hours). The experimental result shows that the Ni-P- 
CNT composite coating has higher corrosion shield compared to Ni-P/nano 
composite coating. It might be due to denser and uniform distribution of 
composite particles with higher phosphorus content. Novakovic and Vassiliou 
[18] have found that, after vacuum heat treatment, a composite coating has less 
corrosion resistance as compared to electroless Ni-P coating and observed the 
same trend for as-deposited Ni-P coating with higher corrosion resistance as 
compared to annealed Ni-P coating.</p>

    <p>To identify the basic characteristics of the corrosion behavior of the coated 
surface in different corrosive environments, the measurement of electrochemical 
corrosion is very essential. From literature review on Ni-P coating, it is 
confirmed that the dissolution of nickel ions occurs at open circuit potential, 
leading to the enrichment of phosphorus on the surface layer. During chemical 
reaction the phosphorus available on the coated surface reacts with water from 
the electrolyte to form a layer of adsorbed hypophosphite anions, which blocks 
the supply of water to the electrode surface and forms a passive nickel film. 
Electroless Ni-P coatings are known as barrier coating, which protects the 
surface of the specimen by sealing it off from corrosive environments. Corrosion 
resistance of the coating also depends on the amorphous structure and passivity 
of the electroless coating. Amorphous alloys offer better corrosion resistance as 
compared to crystalline or polycrystalline materials.</p>

    <p>Different electrochemical tests, namely, potentiodynamic polarization test and 
electrochemical impedance spectroscopy tests are used to study the corrosion 
behavior of electroless nickel coatings. The resistance of the coatings towards 
corrosion is evaluated on the basis of different corrosion parameters obtained 
from such tests such as corrosion potential (E<sub>corr</sub>), corrosion current density 
(I<sub>corr</sub>), charge transfer resistance (R<sub>ct</sub>), double-layer capacitance (C<sub>dl</sub>), and 
corrosion rate (R<sub>c</sub>), etc. The present study deals with the assessment of corrosion 
behavior of Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating using electrochemical impedance 
spectroscopy (EIS) technique. EIS is a non-destructive technique often used to 
understand the corrosion behavior in electrochemical systems and is best suitable 
for the electrochemical characterization of the coating deposited on the metal 
surface. It provides the exhaustive data on the usefulness of coating over a 
relatively small area. It also indicates the occurrence of the rate of corrosion, and 
moisture content in the coating. To maximize the corrosion resistance (R<sub>ct</sub> and 
C<sub>dl</sub>) of the composite coating, the process parameters are optimized in order to 
identify the optimum combination of parameters using Taguchi method with grey 
relational grade. Analysis of variance (ANOVA) is used to observe the level of 
significance of the process parameters and their interactions. The surface 
morphology and composition of Ni-P-Al<sub>2</sub>O<sub>3</sub> coatings are studied with the help 
of scanning electron microscopy (SEM), energy dispersed X-ray analysis (EDX) 
and X-ray diffraction analysis (XRD).</p>


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

    ]]></body>
<body><![CDATA[<p><b><i>Parameters selection and coating deposition</i></b></p>

    <p>Effective deposition of the coating on the surface of the substrate depends on the 
preparation of the substrate. Hence, it is important to prepare the substrate 
surface very carefully and properly. In the present work AISI 1040 (mild steel) of 
size 20 mm &times; 20 mm &times; 2 mm is used as substrate material for Al<sub>2</sub>O<sub>3</sub> composite 
coatings. Different machining processes such as shaping, parting, milling and 
grinding processes are used accordingly for the preparation of the substrate. 
The substrate is mechanically cleaned to remove foreign matters and corrosion 
products, and after that cleaned with de-ionized water. Sequentially a pickling 
treatment is given to the substrate with dilute hydrochloric acid (50 % HCl and 
50% de-ionized water) for short duration of time to remove any surface layer 
formed like rust followed by rinsing with de-ionized water and methanol 
cleaning. To start the coating deposition quickly, the specimen is activated using 
a warm palladium chloride solution, maintained at 55 &deg;C. The activated substrate 
is then dipped into the electroless bath maintained at 85 &deg;C and the coating is 
carried out for three hours duration. For every substrate the constant deposition 
time is maintained to get uniform thickness of the coating. The coating thickness 
is found in the range of 28-32 microns. After the completion of the coating 
deposition process, the samples are cleaned with distilled water and wrapped 
with soft tissue paper.</p>

    <p><a href="#f1">Fig. 1</a> shows the schematic experimental setup for electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> 
composite coating.</p>


    <p>&nbsp;</p>
<a name="f1">
<img src="/img/revistas/pea/v33n1/33n1a06f1.jpg">
    
<p>&nbsp;</p>


    <p>It consists of a heater with a magnetic stirrer (IKA&regr; RCT 
basic). A fixed rigid stand is provided to grip and support the substrate and a 
glass coated temperature sensor. Chemical solution for electroless bath (200 mL) 
is poured into the glass beaker (250 mL size) placed on the heating plate. With 
the help of a temperature sensing knob, the temperature is set at 85 &deg;C and a 
stirrer speed is set with the help of a speed setting knob at 150 rpm. The function 
of PTFE coated magnetic stirrer is to maintain the composite particles in 
suspension without agglomeration at the bottom of the glass beaker. The stirrer 
speed is fixed after a large number of iterations to avoid the decomposition of the 
electroless bath due to the agglomeration of particles.</p>

    <p>The operating conditions and the ranges of chemicals used in electroless bath for 
electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coatings are selected after several trials. The 
three important coating parameters are varied and the others are kept constant for 
coating deposition. The electroless bath composition and operating conditions 
used for the deposition of the electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coatings are 
shown in <a href="#t1">Table 1</a>.</p>


    <p>&nbsp;</p>
<a name="t1">
<img src="/img/revistas/pea/v33n1/33n1a06t1.jpg">
    
<p>&nbsp;</p>


    <p>To have better suspension of the second phase alumina 
particles and to avoid agglomeration of particles, a specified amount of surfactant 
SDS (Sodium Dodecyl Sulphate) is added to the electroless nickel poly alloy 
bath. About 50 mL of electroless nickel solution containing the required amount 
of alumina powder are thoroughly mixed using a Magnetic stirrer (Remi make 
2MLH) to get a uniform suspension of particles in the solution. At first a Ni-P 
layer is deposited in the first hour to prevent the porosity of the coating and then 
the solution containing Al<sub>2</sub>O<sub>3</sub> particles and surfactant is introduced into the same 
bath for subsequent 2 hours for Ni-P-Al<sub>2</sub>O<sub>3</sub> co-deposition.</p>

    ]]></body>
<body><![CDATA[<p>During a chemical reaction within the electroless bath, nickel sulphate, which is 
used as a source of metallic ions, supplies the nickel ions in the solution. In the 
same bath sodium hypophosphite (used as a reducing agent) reduces the nickel 
ions from their positive valence state to zero valence state. At the given 
temperature the chemical reaction between nickel sulphate and sodium 
hypophosphite is quite fast and tremendous, which results in instant 
decomposition of the electroless bath. Consequently, complexing agents (tri 
sodium citrate and sodium acetate) are used to slow down the chemical reaction 
into a feasible form. Complexing agent forms metastable complexes with nickel 
ions and releases them slowly for the reaction, which helps to maintain the 
stability of the electroless bath. Even though the complexing agents have 
performed their duty in the electroless bath, there remains a possibility of 
decomposition of the chemical solution. In such situations the stabilizer (Lead 
acetate) plays an important role in the stabilization of the electroless bath for total 
duration of coating. To increase the wettability and surface charge of alumina 
particles, surfactant Sodium Dodecyl Sulphide is used in the electroless bath. The 
imperative functions of the surfactant are to reduce the surface tension of the 
liquid, easy dispersion of the particles and to reduce the interfacial tension 
between the solid and liquid surfaces. Surfactant reduces the agglomeration of 
the particles and electrostatic adsorption of suspended particles on the substrate 
[19]. To understand the effect of heat treatment on the corrosion resistance of the 
composite coatings, the coated samples are annealed in a box furnace for 1 hour 
at different temperatures (300 &deg;C, 400 &deg;C and 500 &deg;C) according to the 
Orthogonal Array (OA). After annealing, the samples are cooled to room 
temperature without application of any artificial cooling.</p>


    <p><b><i>Parameters optimization process and design of experiments</i></b></p>

    <p>During coating deposition several factors like nickel source concentration, 
reducing agent concentration, pH of the solution, bath temperature, stabilizer and 
surfactant concentration, concentration of second phase particles and substrate 
material affect the coating characteristics. To obtain an optimum combination for 
maximum corrosion resistance, various coating parameters are varied within the 
specific range. From literature review, it is seen that three factors viz. nickel 
suphate (A), sodium hypophosphite (B) and concentration of second phase 
particles, i.e., Al<sub>2</sub>O<sub>3</sub> particles (C), are the most commonly used by the researchers 
to control the properties of the composite coatings [19-21]. Besides, heat 
treatment (annealing) is found to have great effect on the corrosion resistance of 
the coating. Therefore, annealing temperature (D) is consider as the fourth 
parameter in the experimental design to study its effect on the corrosion 
resistance of the coating. The different design factors and their levels are shown 
in <a href="#t2">Table 2</a>.</p>


    <p>&nbsp;</p>
<a name="t2">
<img src="/img/revistas/pea/v33n1/33n1a06t2.jpg">
    
<p>&nbsp;</p>


    <p>The present work considers the optimization of the corrosion behavior of 
electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating using a grey based Taguchi method 
[22] that uses loss function to measure the quality characteristics. The value of 
the loss function is transformed into a statistical measure, called as signal to 
noise ratio (S/N ratio). It is the ratio of the desirable value or signal to standard 
deviation or noise. S/N ratio can effectively consider the variation encountered in 
a set of trials. On the basis of the objective of the experimental work, the S/N 
ratios are classified into three basic criteria: lower-the-better (LB), higher-thebetter 
(HB) and nominal-the-best (NB). A larger S/N ratio represents 
minimization of noise factors. The combination of parameter levels which gives 
a maximum S/N ratio is known as the optimum combination of parameter levels. 
The present work is related to assessment of corrosion characteristics by 
measuring the charge transfer resistance (R<sub>ct</sub>) and double layer capacitance (C<sub>dl</sub>). 
Because of using two different corrosion characteristics, it becomes a complex 
multivariate problem, which cannot be solved by Taguchi method. It may be 
possible that higher S/N ratio of one response variable corresponds to the lower 
S/N ratio of the other. Grey relational analysis [23] is an efficient tool which is 
used for the overall evaluation of the S/N ratio to optimize the multiple response 
characteristics. The optimization of the process is performed in a range of steps. 
In the first step the results of the experiments are normalized in the range of one 
and zero by performing the grey relational generation. In the next step grey 
relational coefficients are calculated with the help of normalized data. The 
normalized data represent the correlation between actual experimental data and 
desired experimental data. In the third step grey the relational grade is calculated 
by averaging the grey relational coefficients. The grey relational grade is treated 
as the overall response of the process instead of multiple responses of charge 
transfer resistance and double layer capacitance.</p>

    <p>A statistical technique, analysis of variance (ANOVA), is performed to find the 
significant parameters of the experiment. The optimum combination of the 
coating process parameters is predicted with the help of ANOVA and grey 
relational analysis. Finally, a confirmation test is conducted to verify the 
optimum process parameters obtained from the analysis. In the present work, 
corrosion behavior of electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating is studied with 
the help of electrochemical impedance spectroscopy. Charge transfer resistance 
(R<sub>ct</sub>) and double layer capacitance (C<sub>dl</sub>) are obtained from the Nyquist plot. R<sub>ct</sub> 
and C<sub>dl</sub> are taken as the response variables for the current study. A higher value 
of R<sub>ct</sub> and lower value of C<sub>dl</sub> indicate better corrosion resistance of the composite 
coating.</p>

    <p>Design of Experiment (DOE) is a systematic and rigorous approach that provides 
the maximum amount of conclusive information from limited experimental runs. 
The DOE of the present study includes an orthogonal array (OA) based on the 
Taguchi method to reduce the number of experiments for the optimization of the 
coating process parameters.</p>

    <p>For successful completion of the experiments it is very essential to choose the 
proper orthogonal array. It allows to compute the total degree of freedom (DOF) 
of main and interaction effects via a minimum number of experimental trials. In 
the present experiment, four process parameters are used with three levels, 
therefore the total DOF considering the individual factors and their interaction is 
20. Hence the L<sub>27</sub> OA is chosen which has 27 rows corresponding to the number 
of experiments and 26 DOF with 13 columns. The L<sub>27</sub> OA is shown in <a href="#t3">Table 3</a>.</p>


    <p>&nbsp;</p>
<a name="t3">
<img src="/img/revistas/pea/v33n1/33n1a06t3.jpg">
    
]]></body>
<body><![CDATA[<p>&nbsp;</p>


    <p>Each row in the table represents the specific combination of the experimental run 
and each column represents a specific factor or interactions. The cell value 
indicates the level of the corresponding factor or interaction assigned to that 
column. The experimental run is controlled by the setting of the design factors 
and not by the interactions.</p>


    <p><b><i>Electrochemical study</i></b></p>

    <p>The electrochemical impedance spectroscopy (EIS) test of heat-treated 
electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coated samples is carried out using a 
potentiostat (Gill AC) of ACM instrument, UK. The test is conducted using 3.5% 
NaCl solution as electrolyte at ambient temperature of 30 &deg;C. The 
electrochemical cell consists of three types of electrodes. A saturated calomel 
electrode (SCE) is used as reference electrode, which provides a stable 
'reference' against which the applied potential may be accurately measured. A 
platinum electrode works as counter electrode or auxiliary electrode, which 
provides the path for the applied current into the solution. The coated specimen is 
used as working electrode. The design of the cell is such that only an area of 1 
cm<sup>2</sup> of the coated surface is exposed to the electrolyte.</p>

    <p><a href="#f2">Fig. 2</a> shows an equivalent electrical circuit model, which is used to arouse and 
fit the corrosion property parameters.</p>


    <p>&nbsp;</p>
<a name="f2">
<img src="/img/revistas/pea/v33n1/33n1a06f2.jpg">
    
<p>&nbsp;</p>


    <p>In the circuit the charge transfer resistance 
(R<sub>ct</sub>) is represented by the resistance of electron transfer during the 
electrochemical reaction course. The double layer capacitance (C<sub>dl</sub>) is correlated 
to delamination of the coating. Solution resistance (Rs) is refered to the resistance 
between the work electrode (WE) and the reference electrode. The values of 
charge transfer resistance and double layer capacitance are calculated from the 
Nyquist plot by fitting a semicircle using the accompanying software.</p>

    <p>The experimental setup of the electrochemical impedance spectroscopy test is 
shown in <a href="#f3">Fig. 3</a>.</p>


    <p>&nbsp;</p>
<a name="f3">
<img src="/img/revistas/pea/v33n1/33n1a06f3.jpg">
    
]]></body>
<body><![CDATA[<p>&nbsp;</p>


    <p>A settling time of 15 minutes is assigned before every test in 
order to stabilize the open circuit potential (OCP). The potentiostat is controlled 
with the help of a sophisticated desktop computer, which also collects and stores 
the data of EIS test. During the test the applied frequency of corrosion setup is 
varied from 10 KHz to 0.01 Hz. The Nyquist plot obtained from the EIS test 
appears in a single semicircle. The semicircle in the high frequency region 
signifies the charge control reaction and is quite consistent [14].</p>


    <p><b><i>Microstructure and characterization study</i></b></p>

    <p>Energy dispersive X-ray analysis (EDAX Corporation) is used to find out and 
verify the weight percentage of nickel, phosphorus, aluminum oxide, and oxygen 
in the composite coating. Scanning electron microscopy (JEOL, JSM-6360) is 
used to observe the surface morphology of the composite coating before and after 
heat treatment. SEM is done in order to investigate the effect of heat treatment on 
the electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coatings. The phase compositions of 
composite coatings before and after heat treatment are detected using an X-ray 
diffraction analyzer (Rigaku, Ultima III).</p>


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

    <p><b><i>Microstructure study and characterization of the Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating</i></b></p>

    <p>SEM micrographs of as-deposited and heat treated Ni-P-Al<sub>2</sub>O<sub>3</sub> composite 
coatings are shown in <a href="#f4">Fig. 4</a>.</p>


    <p>&nbsp;</p>
<a name="f4">
<img src="/img/revistas/pea/v33n1/33n1a06f4.jpg">
    
<p>&nbsp;</p>


    ]]></body>
<body><![CDATA[<p>From the figure it is confirmed that the surface of 
the as-deposited composite coating has a smooth surface with uniform 
distribution of alumina particles with no porosity. The alumina particles are 
properly embedded on the surface of the alloy coating. The uniform distribution 
of the composite particles along with the smooth surface of the coating is due to 
the use of surfactant (SDS) in the electroless bath. After heat treatment of the 
composite coating at 400 &deg;C, the globules of nickel and phosphorus are seen with 
embedded alumina particles. The globules become more compact due to heat 
treatment, which further reduces the porosity of the coating. This may be the 
reason for increase in corrosion resistance of the composite coating.</p>

    <p><a href="#f5">Fig. 5</a> shows the EDAX analysis of as deposited and heat treated Ni-P-Al<sub>2</sub>O<sub>3</sub> 
composite coating.</p>


    <p>&nbsp;</p>
<a name="f5">
<img src="/img/revistas/pea/v33n1/33n1a06f5.jpg">
    
<p>&nbsp;</p>


    <p>The compositional analysis of the coatings deposited at 
different concentrations of nickel sulpahte, sodium hypophosphite, and Al<sub>2</sub>O<sub>3</sub> 
particles is carried out using energy dispersive X-ray analysis. From analysis, it 
is confirmed that the composite coating deposited using 5 g/L of Al<sub>2</sub>O<sub>3</sub> particles 
in the bath has 78.07 wt% of nickel, 6.67 wt% of phosphorus, 8.74 wt% of 
oxygen, and 6.52 wt% of alumina particles. Similarly, the composite coating 
deposited using 10 g/L of Al<sub>2</sub>O<sub>3</sub> particles in the bath has 72.46 wt% of nickel, 
6.92 wt% of phosphorus, 11.06 wt% of oxygen, and 9.56 wt% of alumina 
particles. It means that the amount of alumina particles in the composite coating 
increases with increase in Al<sub>2</sub>O<sub>3</sub> particles in the electroless bath. </p>

    <p>X-ray diffraction (XRD) analyzer (Rigaku, Ultima III) is used for identification 
of different compounds in the electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating. 
<a href="#f6">Fig. 6</a> shows XRD plots of as deposited and heat treated composite coatings.</p>


    <p>&nbsp;</p>
<a name="f6">
<img src="/img/revistas/pea/v33n1/33n1a06f6.jpg">
    
<p>&nbsp;</p>


    <p>From the 
plots it is confirmed that in as-deposited condition the phase is mostly amorphous 
in nature, as a single broad peak is available at diffraction angle of 44.468. After 
heat treatment at 400 &deg;C for one hour, the amorphous phase of composite coating 
is converted into crystalline phase. Different peaks are seen at different 
diffraction angles. The highest peak of Ni3P with Al<sub>2</sub>O<sub>3</sub> is observed at the 
diffraction angle of 44.320. Ni3P peaks are also observed at the diffraction angles 
of 43.1, 43.5, 43.74, 44.26, 45.04 and peaks of Al<sub>2</sub>O<sub>3</sub> are observed at diffraction 
angles of 37.06, 53.46, 55.7, and 77.28. Similarly, peaks of Ni are observed at 
diffraction angles of 52.18, and 77.38.</p>


    <p><b><i>Coating process parameter optimization and confirmation test</i></b></p>

    ]]></body>
<body><![CDATA[<p>The present work deals with two responses, charge transfer resistance and double 
layer capacitance, for optimization of the corrosion resistance of Ni-P-Al<sub>2</sub>O<sub>3</sub> 
composite coatings. Grey analysis is a technique which converts a multi 
response (variable) problem into a single response problem. The experimental 
data for charge transfer resistance (R<sub>ct</sub>) and double layer capacitance (C<sub>dl</sub>) of the 
electrochemical impedance test are given in <a href="#t4">Table 4</a>.</p>


    <p>&nbsp;</p>
<a name="t4">
<img src="/img/revistas/pea/v33n1/33n1a06t4.jpg">
    
<p>&nbsp;</p>


    <p>The particular sets of 
analysis are performed to convert the given multiple responses into a single 
performance index, called as grey relational grade.</p>

    <p>Experimental results of the linear normalization, i.e., charge transfer resistance 
and double layer capacitance in the range of zero and one are vital for generating 
the grey relational coefficient. A material will have a lower tendency to corrode 
if R<sub>ct</sub> value tends to be a higher and C<sub>dl</sub> to be a lower value. 
From <a href="#t4">Table 4</a> it is 
observed that the values of charge transfer resistance for all experiments are 
positive, hence higher the better criterion is used for normalization. Similarly, for 
all values of double layer capacitance lower the better criterion is used. 
The expressions for higher the better and lower the better criterion are given 
below.</p>

    <p>Equation for higher the better:</p>


    <p>&nbsp;</p>
<a name="e1">
<img src="/img/revistas/pea/v33n1/33n1a06e1.jpg">
    
<p>&nbsp;</p>


    <p>Equation for lower the better:</p>


    <p>&nbsp;</p>
<a name="e2">
<img src="/img/revistas/pea/v33n1/33n1a06e2.jpg">
    
]]></body>
<body><![CDATA[<p>&nbsp;</p>


    <p>where x<sub>i</sub>(k) is the value after grey relational generation, while min y<sub>i</sub>(k) 
and max y<sub>i</sub>(k) are the smallest and largest values of y<sub>i</sub>(k) 
for the k<sub>th</sub> response. The data after grey relational grade are shown in <a href="#t5">Table 5</a>.</p>


    <p>&nbsp;</p>
<a name="t5">
<img src="/img/revistas/pea/v33n1/33n1a06t5.jpg">
    
<p>&nbsp;</p>


    <p>The grey relational coefficient is calculated from the normalized value and the 
equation for the grey relational coefficient is as follows.</p>


    <p>&nbsp;</p>
<a name="e3">
<img src="/img/revistas/pea/v33n1/33n1a06e3.jpg">
    
<p>&nbsp;</p>


    <p>where &Delta;<sub>0i</sub> = &#8741; x<sub>0</sub>(k) - x<sub>i</sub>(k) &#8741;
is the difference of the absolute value between x<sub>0</sub>(k) and x<sub>i</sub>(k). 
&Delta;<sub>min</sub> and &Delta;<sub>max</sub> are the minimum and maximum values of the absolute 
differences (&Delta;<sub>0i</sub>) of all comparing sequences. The overall multiple response 
characteristics evaluation is based on the grey relational grade and is calculated 
as follows:</p>


    <p>&nbsp;</p>
<a name="e4">
<img src="/img/revistas/pea/v33n1/33n1a06e4.jpg">
    
<p>&nbsp;</p>


    ]]></body>
<body><![CDATA[<p>where n is the number of process responses. The grey relational grades are 
considered in the optimization of multi-response parameter design problem. The 
values of grey relational grade are shown in <a href="#t6">Table 6</a>.</p>


    <p>&nbsp;</p>
<a name="t6">
<img src="/img/revistas/pea/v33n1/33n1a06t6.jpg">
    
<p>&nbsp;</p>


    <p>As the grey relational grade is to maximized, the S/N ratio is calculated using 
higher the better criterion which is given by:</p>


    <p>&nbsp;</p>
<a name="e5">
<img src="/img/revistas/pea/v33n1/33n1a06e5.jpg">
    
<p>&nbsp;</p>


    <p>where y is the observed data and n is the number of observations. As the 
experimental design is orthogonal, it is possible to separate out the effect of each 
coating parameter at different levels. The mean grey relational grade for three 
levels of the four factors is summarized in <a href="#t7">Table 7</a>.</p>


    <p>&nbsp;</p>
<a name="t7">
<img src="/img/revistas/pea/v33n1/33n1a06t7.jpg">
    
<p>&nbsp;</p>


    <p>All the calculations are 
performed with the help of Minitab software [24]. The response table shows the 
average of the selected characteristic for each level of the factors. The ranks 
shown in the table are based on Delta statistics and it compares the relative 
magnitude of effects. The Delta statistics is the difference of highest average and 
lowest average of each factor. Ranks are assigned on the basis of Delta values; 
rank 1 is assigned to the highest Delta value, rank 2 is assigned to next highest 
value, and so on. <a href="#f7">Fig. 7</a> shows the main effects plot for mean 
S/N ratio and <a href="#f8">Fig. 8</a> shows the interaction plots between the process parameters.</p>


    ]]></body>
<body><![CDATA[<p>&nbsp;</p>
<a name="f7">
<img src="/img/revistas/pea/v33n1/33n1a06f7.jpg">
    
<p>&nbsp;</p>
<a name="f8">
<img src="/img/revistas/pea/v33n1/33n1a06f8.jpg">
    
<p>&nbsp;</p>


    <p>If the line for a particular parameter in the main effect plot is horizontal, it means 
that the parameter has no significant effect. On the other hand, if the line has 
maximum inclination to horizontal line, it means that the parameter has the most 
significant effect. From <a href="#f7">Fig. 7</a> it is clear that annealing temperature (parameter 
D) has a significant effect, the concentration of Al<sub>2</sub>O<sub>3</sub> particles (parameter C) has 
the most significant effect and the reducing agent (parameter B) has a moderate 
significant effect. Parameter A is less significant due to less inclination to the 
horizontal line. Increase in the corrosion resistance of the composite coating in 
the presence of Al<sub>2</sub>O<sub>3</sub> particles has also been observed earlier. In Ni-P-(Al<sub>2</sub>O<sub>3</sub>- 
TiC) composite coating, the corrosion resistance is increased in presence of 
Al<sub>2</sub>O<sub>3</sub> particles upto a certain level of particle concentration in the bath and after 
that it gets decreased [6]. In a further case [3], the researchers have observed that 
the corrosion resistance is increased with increase in Al<sub>2</sub>O<sub>3</sub> particles. 
Interactions between parameters A, B and C are shown in <a href="#f8">Fig. 8</a>. From the plots 
it is observed that almost all lines are intersecting to each other, i.e., all factors 
have some amount of interaction between each other. From the figure it is seen a 
considerable interaction between parameters B and C and between parameters A 
and C. Thus, from the present analysis, it is confirmed that annealing temperature 
and concentration of Al<sub>2</sub>O<sub>3</sub> particles are the significant parameters for the 
corrosion characteristics of Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coatings. In Taguchi method, 
optimum level of combinations is selected for those levels, which are having 
higher S/N ratios. In the present study the optimal combination is found to be 
A1B3C3D3.</p>

    <p>ANOVA is useful to investigate the effect of the process parameters and of their 
significance level. This technique gives various important conclusions based on 
analysis of the experimental data. ANOVA separates the total variability of the 
response into contribution of each of the factors and the error. A sophisticated 
software Minitab is used to obtain the results through ANOVA with the S/N 
ratio. ANOVA results for the corrosion behavior of the composite coatings are 
shown in <a href="#t8">Table 8</a>.</p>


    <p>&nbsp;</p>
<a name="t8">
<img src="/img/revistas/pea/v33n1/33n1a06t8.jpg">
    
<p>&nbsp;</p>


    <p>ANOVA calculations are based on the F-ratio or variance 
ratio. It is used to measure the significance of the parameters under investigation 
with respect to variations of all the terms included in the error term at the desired 
significance level. If the calculated value is higher than the tabulated one, the 
factor is significant at the desired level. The ANOVA table shows the percentage 
contribution of each parameter. From the table it is observed that parameter C 
(concentration of Al<sub>2</sub>O<sub>3</sub> particles) has the most significant effect on the corrosion 
behavior at the confidence level of 95% within the specific test range. The 
annealing temperature (D) and concentration of reducing agent (B) are 
significant at 90% confidence level. Among the interactions, the interaction of 
parameters between B and C has a significant contribution. The percentage 
contribution of the factors and interactions are calculated to know the influence 
of the process parameters. From ANOVA table it is clear that parameter C has 
the largest contribution (23.071%) followed by parameter C (20.50%). Among 
interactions, B&times;C interaction has the highest contribution (9.74%). 
In the final step, confirmation results of optimum parameters are calculated by 
Taguchi method. The confirmation test is performed by conducting the 
experiment with optimal settings of the factors and levels previously calculated.</p>

    <p>The predicted values of the S/N ratio at the optimum level his calculated as</p>


    <p>&nbsp;</p>
<a name="e5">
<img src="/img/revistas/pea/v33n1/33n1a06e5.jpg">
    
]]></body>
<body><![CDATA[<p>&nbsp;</p>


    <p>where &eta;m is the total mean grey relational grade, hiis the mean grey relational 
grade at optimal level, and 'o' is the number of main design parameters that 
significantly affect the corrosion resistance of Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coating. 
The results of the validation test are shown in <a href="#t9">Table 9</a>.</p>


    <p>&nbsp;</p>
<a name="t9">
<img src="/img/revistas/pea/v33n1/33n1a06t9.jpg">
    
<p>&nbsp;</p>


    <p>The significant 
improvement in grey relational grade from initial to optimum condition is 
0.2768, which is about 41.21% of the mean relational grade. Nyquist plots for the 
Ni-P-Al<sub>2</sub>O<sub>3</sub> composite coatings developed at initial and optimal condition are 
shown in <a href="#f9">Fig. 9</a>.</p>


    <p>&nbsp;</p>
<a name="f9">
<img src="/img/revistas/pea/v33n1/33n1a06f9.jpg">
    
<p>&nbsp;</p>


    <p>From the plots it is confirmed that the semicircle for optimum condition is larger 
than that of initial condition. Therefore the corrosion resistance at optimum 
condition is higher than that of initial condition.</p>


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

    ]]></body>
<body><![CDATA[<p>Taguchi method in combination with grey relational analysis is used in order to 
optimize the electrochemical parameters of electroless Ni-P-Al<sub>2</sub>O<sub>3</sub> composite 
coating using electrochemical impedance spectroscopy test in 3.5% NaCl 
solution. The optimum parameter combination is found to be A1B3C3D3. At 
optimum combination, the nickel concentration is 35 g/L, the reducing agent 
concentration is 25 g/L, the concentration of Al<sub>2</sub>O<sub>3</sub> particles is 15 g/L, and the 
annealing temperature is 500 &deg;C. From ANOVA results it is confirmed that the 
concentration of Al<sub>2</sub>O<sub>3</sub> particles and the annealing temperature have the most 
significant influence on corrosion resistance of the composite coating. The 
interaction between the reducing agent and the concentration of Al<sub>2</sub>O<sub>3</sub> particles 
has good significant effect among the interactions. The corrosion resistance of 
the composite coating improves with increase in alumina content and annealing 
temperature at 500 &deg;C. The improvement in the grey relational grade from initial 
condition to optimal condition is found to be 41.21%. The coating composition is 
studied using EDX analysis. The micro structural analysis and crystallization 
behavior of the coating is studied with the help of SEM and XRD analysis. From 
SEM micrograph, it is confirmed that the alumina particles are uniformly 
distributed over the smooth coated surface without porosity. From EDX analysis, 
it is confirmed that the coating is deposited with the alumina particles, nickel, 
phosphorus and oxygen. From XRD plots it is confirmed that the as deposited 
composite coating has amorphous structure and it converts into a crystalline 
structure after heat treatment at 400 &deg;C with Ni3P as a major compound.</p>


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

    <!-- ref --><p>1. Balaraju J N, Sankara Narayanan T S N, Seshadri S K. J Appl Electrochem. 2003;33:807.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000126&pid=S0872-1904201500010000600001&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>2. Sudagar J, Lian J, Sha W. J Alloys Comp. 2013;571:183.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000128&pid=S0872-1904201500010000600002&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>3. Sharma A, Singh AK. J Mater Eng Perform. 2013;22:176.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000130&pid=S0872-1904201500010000600003&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>4. Sahoo P, Das SK. Mater Design. 2011;32:1760.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000132&pid=S0872-1904201500010000600004&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>5. Apachitei I, Tichelaar F D, Duszczyk J, et al. Surf Coat Techn. 2001;148:284.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000134&pid=S0872-1904201500010000600005&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>6. Abdel Aal A, Zaki Z I, Hamid Z A. Mater Sci Eng A. 2007;447:87.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000136&pid=S0872-1904201500010000600006&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>7. Balaraju J N, Sankara Narayanan T S N, et al. Mater Res Bull. 2006;41:847.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000138&pid=S0872-1904201500010000600007&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>8. Alirezaei Sh, Monirvaghefi S M, Salehi M, et al. Surf Coat Technol. 2004;184:170.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000140&pid=S0872-1904201500010000600008&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>9. Riedel W. Electroless nickel plating. UK: Finishing Publications Ltd; 1991.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000142&pid=S0872-1904201500010000600009&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>10. Hamdy A S, Shoieb M A, Hady H, et al. Surf Coat Technol. 2007;202:162.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000144&pid=S0872-1904201500010000600010&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>11. Bigdeli F, Allahkaram S R. Mater Design. 2009;30:4450.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000146&pid=S0872-1904201500010000600011&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>12. Zarebidaki A, Allahkaram SR. Micro Nano Lett. 2011;6:937.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000148&pid=S0872-1904201500010000600012&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>13. Stankiewicz A, Masalski J, Szczygiel B. Mater Corros. 2013;64:908.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000150&pid=S0872-1904201500010000600013&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>14. Allahkaram S R, Zoughi M, Rabizadeh T. Micro Nano Lett. 2010;5:262.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000152&pid=S0872-1904201500010000600014&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>15. Praveen B M, Venkatesha T V, Naik Y A, et al. Surf Coat Technol. 2007;201:5836.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000154&pid=S0872-1904201500010000600015&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>16. Zarebidaki A, Allahkaram S R. Micro Nano Lett. 2012;7:90.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000156&pid=S0872-1904201500010000600016&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>17. Lee CK. Int J Electrochem Sci. 2012;7:12941.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000158&pid=S0872-1904201500010000600017&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>18. Novakovic J, Vassiliou P. Electrochim Acta. 2009;54:2499.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000160&pid=S0872-1904201500010000600018&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>19. Liu D, Yan Y, Lee K, et al. Mater Corros. 2009;60:690.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000162&pid=S0872-1904201500010000600019&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>20. Sahoo P. J Phys D: Appl Phys. 2008;41:95305.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000164&pid=S0872-1904201500010000600020&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>21. Das SK, Sahoo P. Adv Mechanical Eng. 2012;703168:1.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000166&pid=S0872-1904201500010000600021&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>22. Roy RK. A Primer on the Taguchi Method. Mich, USA: Dearborn Society of Manufacturing Engineers; 1990.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000168&pid=S0872-1904201500010000600022&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>23. Deng J. J Grey System. 1989;1:1.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000170&pid=S0872-1904201500010000600023&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>

    <!-- ref --><p>24. Minitab user manual (release 13.2). Making data analysis easier, MINITAB Incorporation, State College, PA, USA. 2001.    &nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;[&#160;<a href="javascript:void(0);" onclick="javascript: window.open('/scielo.php?script=sci_nlinks&ref=000172&pid=S0872-1904201500010000600024&lng=','','width=640,height=500,resizable=yes,scrollbars=1,menubar=yes,');">Links</a>&#160;]<!-- end-ref --></p>


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

    <p>Received 9 February 2015; accepted 25 February 2015</p>

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


     ]]></body><back>
<ref-list>
<ref id="B1">
<label>1</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Balaraju]]></surname>
<given-names><![CDATA[J N]]></given-names>
</name>
<name>
<surname><![CDATA[Sankara Narayanan]]></surname>
<given-names><![CDATA[T S N]]></given-names>
</name>
<name>
<surname><![CDATA[Seshadri]]></surname>
<given-names><![CDATA[S K]]></given-names>
</name>
</person-group>
<source><![CDATA[J Appl Electrochem]]></source>
<year>2003</year>
<volume>33</volume>
<page-range>807</page-range></nlm-citation>
</ref>
<ref id="B2">
<label>2</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sudagar]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Lian]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Sha]]></surname>
<given-names><![CDATA[W]]></given-names>
</name>
</person-group>
<source><![CDATA[J Alloys Comp]]></source>
<year>2013</year>
<volume>571</volume>
<page-range>183</page-range></nlm-citation>
</ref>
<ref id="B3">
<label>3</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sharma]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[Singh]]></surname>
<given-names><![CDATA[A K]]></given-names>
</name>
</person-group>
<source><![CDATA[J Mater Eng Perform]]></source>
<year>2013</year>
<volume>22</volume>
<page-range>176</page-range></nlm-citation>
</ref>
<ref id="B4">
<label>4</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sahoo]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
<name>
<surname><![CDATA[Das]]></surname>
<given-names><![CDATA[S K]]></given-names>
</name>
</person-group>
<source><![CDATA[Mater Design]]></source>
<year>2011</year>
<volume>32</volume>
<page-range>1760</page-range></nlm-citation>
</ref>
<ref id="B5">
<label>5</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Apachitei]]></surname>
<given-names><![CDATA[I]]></given-names>
</name>
<name>
<surname><![CDATA[Tichelaar]]></surname>
<given-names><![CDATA[F D]]></given-names>
</name>
<name>
<surname><![CDATA[Duszczyk]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
</person-group>
<source><![CDATA[Surf Coat Techn]]></source>
<year>2001</year>
<volume>148</volume>
<page-range>284</page-range></nlm-citation>
</ref>
<ref id="B6">
<label>6</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Abdel Aal]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[Zaki]]></surname>
<given-names><![CDATA[Z I]]></given-names>
</name>
<name>
<surname><![CDATA[Hamid]]></surname>
<given-names><![CDATA[Z A]]></given-names>
</name>
</person-group>
<source><![CDATA[Mater Sci Eng A]]></source>
<year>2007</year>
<volume>447</volume>
<page-range>87</page-range></nlm-citation>
</ref>
<ref id="B7">
<label>7</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Balaraju]]></surname>
<given-names><![CDATA[J N]]></given-names>
</name>
<name>
<surname><![CDATA[Sankara Narayanan]]></surname>
<given-names><![CDATA[T S N]]></given-names>
</name>
</person-group>
<source><![CDATA[Mater Res Bull]]></source>
<year>2006</year>
<volume>41</volume>
<page-range>847</page-range></nlm-citation>
</ref>
<ref id="B8">
<label>8</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Alirezaei]]></surname>
<given-names><![CDATA[Sh]]></given-names>
</name>
<name>
<surname><![CDATA[Monirvaghefi]]></surname>
<given-names><![CDATA[S M]]></given-names>
</name>
<name>
<surname><![CDATA[Salehi]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
</person-group>
<source><![CDATA[Surf Coat Technol]]></source>
<year>2004</year>
<volume>184</volume>
<page-range>170</page-range></nlm-citation>
</ref>
<ref id="B9">
<label>9</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Riedel]]></surname>
<given-names><![CDATA[W]]></given-names>
</name>
</person-group>
<source><![CDATA[Electroless nickel plating]]></source>
<year>1991</year>
<publisher-name><![CDATA[Finishing Publications Ltd]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B10">
<label>10</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Hamdy]]></surname>
<given-names><![CDATA[A S]]></given-names>
</name>
<name>
<surname><![CDATA[Shoieb]]></surname>
<given-names><![CDATA[M A]]></given-names>
</name>
<name>
<surname><![CDATA[Hady]]></surname>
<given-names><![CDATA[H]]></given-names>
</name>
</person-group>
<source><![CDATA[Surf Coat Technol]]></source>
<year>2007</year>
<volume>202</volume>
<page-range>162</page-range></nlm-citation>
</ref>
<ref id="B11">
<label>11</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Bigdeli]]></surname>
<given-names><![CDATA[F]]></given-names>
</name>
<name>
<surname><![CDATA[Allahkaram]]></surname>
<given-names><![CDATA[S R]]></given-names>
</name>
</person-group>
<source><![CDATA[Mater Design]]></source>
<year>2009</year>
<volume>30</volume>
<page-range>4450</page-range></nlm-citation>
</ref>
<ref id="B12">
<label>12</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zarebidaki]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[Allahkaram]]></surname>
<given-names><![CDATA[S R]]></given-names>
</name>
</person-group>
<source><![CDATA[Micro Nano Lett]]></source>
<year>2011</year>
<volume>6</volume>
<page-range>937</page-range></nlm-citation>
</ref>
<ref id="B13">
<label>13</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Stankiewicz]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[Masalski]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Szczygiel]]></surname>
<given-names><![CDATA[B]]></given-names>
</name>
</person-group>
<source><![CDATA[Mater Corros]]></source>
<year>2013</year>
<volume>64</volume>
<page-range>908</page-range></nlm-citation>
</ref>
<ref id="B14">
<label>14</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Allahkaram]]></surname>
<given-names><![CDATA[S R]]></given-names>
</name>
<name>
<surname><![CDATA[Zoughi]]></surname>
<given-names><![CDATA[M]]></given-names>
</name>
<name>
<surname><![CDATA[Rabizadeh]]></surname>
<given-names><![CDATA[T]]></given-names>
</name>
</person-group>
<source><![CDATA[Micro Nano Lett]]></source>
<year>2010</year>
<volume>5</volume>
<page-range>262</page-range></nlm-citation>
</ref>
<ref id="B15">
<label>15</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Praveen]]></surname>
<given-names><![CDATA[B M]]></given-names>
</name>
<name>
<surname><![CDATA[Venkatesha]]></surname>
<given-names><![CDATA[T V]]></given-names>
</name>
<name>
<surname><![CDATA[Naik]]></surname>
<given-names><![CDATA[Y A]]></given-names>
</name>
</person-group>
<source><![CDATA[Surf Coat Technol]]></source>
<year>2007</year>
<volume>201</volume>
<page-range>5836</page-range></nlm-citation>
</ref>
<ref id="B16">
<label>16</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Zarebidaki]]></surname>
<given-names><![CDATA[A]]></given-names>
</name>
<name>
<surname><![CDATA[Allahkaram]]></surname>
<given-names><![CDATA[S R]]></given-names>
</name>
</person-group>
<source><![CDATA[Micro Nano Lett]]></source>
<year>2012</year>
<volume>7</volume>
<page-range>90</page-range></nlm-citation>
</ref>
<ref id="B17">
<label>17</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lee]]></surname>
<given-names><![CDATA[C K]]></given-names>
</name>
</person-group>
<source><![CDATA[Int J Electrochem Sci]]></source>
<year>2012</year>
<volume>7</volume>
<page-range>12941</page-range></nlm-citation>
</ref>
<ref id="B18">
<label>18</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Novakovic]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
<name>
<surname><![CDATA[Vassiliou]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<source><![CDATA[Electrochim Acta]]></source>
<year>2009</year>
<volume>54</volume>
<page-range>2499</page-range></nlm-citation>
</ref>
<ref id="B19">
<label>19</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Liu]]></surname>
<given-names><![CDATA[D]]></given-names>
</name>
<name>
<surname><![CDATA[Yan]]></surname>
<given-names><![CDATA[Y]]></given-names>
</name>
<name>
<surname><![CDATA[Lee]]></surname>
<given-names><![CDATA[K]]></given-names>
</name>
</person-group>
<source><![CDATA[Mater Corros]]></source>
<year>2009</year>
<volume>60</volume>
<page-range>690</page-range></nlm-citation>
</ref>
<ref id="B20">
<label>20</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sahoo]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<source><![CDATA[J Phys D: Appl Phys]]></source>
<year>2008</year>
<volume>41</volume>
<page-range>95305</page-range></nlm-citation>
</ref>
<ref id="B21">
<label>21</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Das]]></surname>
<given-names><![CDATA[S K]]></given-names>
</name>
<name>
<surname><![CDATA[Sahoo]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<source><![CDATA[Adv Mechanical Eng]]></source>
<year>2012</year>
<volume>703168</volume>
<page-range>1</page-range></nlm-citation>
</ref>
<ref id="B22">
<label>22</label><nlm-citation citation-type="book">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Roy]]></surname>
<given-names><![CDATA[R K]]></given-names>
</name>
</person-group>
<source><![CDATA[A Primer on the Taguchi Method]]></source>
<year>1990</year>
<publisher-loc><![CDATA[^eMich Mich]]></publisher-loc>
<publisher-name><![CDATA[Dearborn Society of Manufacturing Engineers]]></publisher-name>
</nlm-citation>
</ref>
<ref id="B23">
<label>23</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Deng]]></surname>
<given-names><![CDATA[J]]></given-names>
</name>
</person-group>
<source><![CDATA[J Grey System]]></source>
<year>1989</year>
<volume>1</volume>
<page-range>1</page-range></nlm-citation>
</ref>
<ref id="B24">
<label>24</label><nlm-citation citation-type="book">
<source><![CDATA[Minitab user manual: Making data analysis easier]]></source>
<year>2001</year>
<publisher-loc><![CDATA[^ePA PA]]></publisher-loc>
<publisher-name><![CDATA[MINITAB Incorporation, State College]]></publisher-name>
</nlm-citation>
</ref>
</ref-list>
</back>
</article>
