The Corrosion Resistance of Nickel Electrocomposite Coating Containing BaFe12O19 Particles
Electroplating composite coating is an effective method to prepare composite coating through the codeposition of metallic, nonmetallic, or polymer particles with metal to improve properties such as corrosion resistance, hardness, and wear performance. This paper reports the synthesis of a novel Ni-BaFe12O19 magnetic nanocomposite coating exhibiting improved corrosion resistance. In the present paper, BaFe12O19 particles were synthesized by a single-step solution combustion method and characterized for phase, particle size, and morphology. These particles were incorporated in a nickel metal matrix, and the properties of the coatings like nanohardness and corrosion resistance were investigated. The coating microstructure was also studied using field emission scanning electron microscope. A Vickers hardness of 777 HV was exhibited by Ni-BaFe12O19, and plain Ni coating exhibited a hardness of 517 HV. The Ni-BaFe12O19 composite coating exhibited improved corrosion resistance compared to plain Ni coating with an value of 0.034 μA/cm2 compared to 0.361 μA/cm2 for plain Ni. The Ni-BaFe12O19 coating also exhibited higher charge transfer and polarization resistance compared to plain Ni coating.
In recent years, there is an increased interest in the synthesis and properties of particle reinforced metal matrix nanocomposite coatings with grain size of both matrix and dispersed particles less than 100 nm . Particle-reinforced metal matrix composite (MMC) coatings have been widely used in various engineering applications due to their excellent mechanical, wear, and corrosion resistant properties compared to their components . In composite materials, the metal matrix properties are modified by the addition of various insoluble substances like hard oxides (, , , , and ); carbides (SiC and WC); diamond or solid lubricants (graphite, , or PTFE) [2, 3]. Electrocodeposition is a coating protective technique which consists of introducing homogeneously dispersing inert particles of a different material in the metal matrix; this two-phase coating improves corrosion, wear, and mechanical resistance. The improvement of these properties depends on the combination of both particles and metal matrix. This method has the following advantages like low cost, low temperature and single-step process without additional thermal treatment . The application of magnetic particles in electrodeposited composite coatings is less explored. Barium ferrite thin film media are attractive candidates for high-density overcoat free magnetic recording due to their large uniaxial anisotropy, high chemical stability, and corrosion resistance . Thin films and micromagnets arrays of a composite matrix consisting of magnetic particles and a ferromagnetic alloy have been fabricated based on magnetic composite electroplating. Guan and Nelson have reported the fabrication of arrays of CoNiP-BaFe12O19 magnets with a variety of dimensions and features as small as 8 μm . Qu and Jiao also reported the fabrication of CoNiMnP-BaFe12O19 magnetic composite coating by electrodeposition for applications in microelectromechanical systems actuators. This coating exhibited a maximum magnetic energy density of 17.68 kJm−3 and maximum coercivity of 1342 Oe . However, to the best of our knowledge, there are no reports on the application of barium hexaferrite particles for improving the corrosion resistance of electrodeposited Ni-metal matrix composites. The main aim of the present work is to prepare barium hexaferrite magnetic particles and incorporate them in Ni-metal matrix and study the corrosion resistance and microstructure of the composite coating.
2.1. Preparation and Characterization of Barium Hexaferrite Powder
The solution combustion method is a very versatile technique that has been used for the preparation of magnetic oxides and in particular ferrites . Barium hexaferrite powder was prepared by the solution combustion method as follows: an aqueous redox mixture containing stoichiometric amounts of barium nitrate (5.39 g), ferric nitrate (100 g), and 46.33 g of oxalyl dihydrazide (ODH) was dissolved in minimum amounts of water and transferred into an alumina crucible and placed in a muffle furnace. The oxidizer-to-fuel ratio was maintained as unity. The temperature of the furnace was raised to and then switched off. The solution boils, undergoes frothing, and undergoes smoldering type combustion with low intensity sparks. This is followed by the evolution of copious amounts of gases and results in a brown voluminous mass. The obtained brown voluminous mass was the hard magnetic barium hexaferrite particles (Figure 1(a)). The as-prepared powder was magnetic in nature (Figure 1(b)).
Assuming complete combustion, the theoretical equation for the formation of barium ferrite using ODH can be written as follows: For every mole of BaFe12O19 formed 152 moles of gases were evolved. The powder was characterized by powder X-ray diffractometer (Bruker D8, Advance), particle size analyzer (Mastersizer 2000, Malvern Instruments), and field emission scanning electron microscope (FESEM, Carl Zeiss Supra 40 VP).
2.2. Preparation of Ni-BaFe12O19 Composite Coatings
Nickel sulfamate plating bath was prepared by mixing 300 g L−1 of nickel sulfamate solution (50 g of nickel per liter), 10 g L−1 of nickel chloride, 30 g L−1 boric acid, and 0.2 g L−1 of sodium lauryl sulfate. The Ni-sulfamate plating bath (approximately 200 mL) containing BaFe12O19 particles (5 g/L) was taken in a glass beaker and was mechanically stirred overnight. For higher bath loadings, the electrolyte bath was saturated with powders because of its very fine nature, and there was no coating formation, and hence 5 g/L of barium hexaferrite particles was chosen. During electrodeposition, the bath was held at room temperature, and its pH was maintained at 4 by the addition of sulfamic acid and basic nickel carbonate. A pure nickel sheet () and a brass substrate of the same dimension were used as anode and cathode of respectively. The polished brass substrate of area was degreased with acetone followed by cathodic cleaning and acid dipping and finally washed with distilled water. In order to ensure uniform dispersion of the powder, the electrolyte bath containing particles was subjected to mechanical agitation for 15 hours before the deposition process, and during electrodeposition the particles were also mechanically stirred at a fixed rpm. The codeposition was carried out at 1.55 Adm−2 for 3 h such that the deposit thickness was approximately 40 μm based on Faraday’s laws.
2.3. Characterization of Ni-BaFe12O19 Composite Coatings
2.3.1. XRD, Nanohardness, and Microstructural Studies of BaFe12O19 Composite Coatings
The XRD patterns of plain Ni and Ni-BaFe12O19 composite coatings electrodeposited at 1.55 A dm−2 were also recorded. The metallographic specimens for cross-sectional studies were prepared by sandwiching electrodeposited Ni-BaFe12O19 brass coupons with a copper backup in a Bakelite matrix followed by mechanical grinding and polishing with slurry, down to 0.05 μm. The nanohardness was obtained on electrodeposited Ni and Ni-BaFe12O19 cross-sections using CSM Instruments using the Oliver Pharr method. A Berkovich diamond indenter with 200 mN load was used for the measurements. The surface FESEM images of plain Ni and Ni-BaFe12O19 coatings were also recorded.
2.3.2. Corrosion Studies
Corrosion behavior of Ni and Ni-BaFe12O19 composite coatings electrodeposited at 1.55 A dm−2 for 45 min on mild steel coupons was conducted using CHI 604 2D electrochemical workstation. The test was carried out in deaerated 3.5 wt% (0.6 M) NaCl solution () using conventional three-electrode cell equipped with coated brass coupon with an active area of 1 cm2 as working electrode and platinum foil and saturated calomel electrode (SCE) used as counter and reference electrodes, respectively. The reference electrode was connected to a Luggin capillary, and its tip was placed very close to the surface of the working electrode to minimize IR drop. The coupon was immersed in NaCl solution for an hour in order to establish the open circuit potential (EOCP). Electrochemical Impedance Spectroscopy (EIS) studies were carried out in the frequency range of 100 kHz–10 mHz. The amplitude of applied alternating potential was 10 mV on the EOCP. The impedance data was displayed as Nyquist and Bode plots, respectively. The Nyquist plot is a plot of real () versus imaginary impedance (). The Bode plot is a plot of versus frequency and frequency versus phase angle (), where is the absolute impedance. The acquired data were curve-fitted and analyzed using ZSimpWin program. After EIS measurements, the system was allowed to attain open circuit potential, then the upper and lower potential limits of linear sweep voltammetry were set at with respect to the EOCP. The sweep rate was 1 mV/s. The Tafel plots obtained have been represented as potential versus plot.
The corrosion potential , corrosion current density , and polarization resistance were deduced from the Tafel plot. The polarization resistance was obtained using the Stern-Geary equation:where and are the Tafel slopes or the Tafel constants, expressed in mV/dec.
Corrosion rates (CR) were calculated by the following equation:
3. Results and Discussion
3.1. Powder Characterization
The as-prepared BaFe12O19 powder was poorly crystalline as seen from the XRD pattern (Figure 2).
And hence it was not possible to determine the crystallite size. However, the phase purity of the sample was indirectly evident from the strong magnetic behavior of the as-prepared BaFe12O19 powder (Figure 1). Further calcinations of the barium ferrite will result in crystalline powder as reported in the literature .
The powder morphology of the combustion synthesized barium ferrite powder was analyzed by field emission scanning electron microscopy (FESEM) (Figure 3). From the FESEM image, it is evident that the particles are forming flakes and some hexagonal shaped particles mostly in nanosize were observed.
The particle size analysis of BaFe12O19 powder prepared by solution combustion method is shown in Figure 4. The particles have a tendency to agglomerate, and this is evident from the particle size analysis. The particle size distribution curve showed a Gaussian distribution with an average agglomerated particle size of 5.3 μm.
3.2. Ni-BaFe12O19 Composite Coating
The XRD patterns of Ni and Ni-BaFe12O19 electrocomposite coatings are shown in Figure 5, and the peaks were very sharp in case of plain Ni. The XRD patterns show the peaks corresponding to plain Ni, and no peaks corresponding to BaFe12O19 were observed as the percentage of particles incorporated is less than 5 wt% and also due to the poorly crystalline nature of the powder. Also, there was no change in the orientation of Ni peaks with the particle incorporation.
FESEM images of electrodeposited plain Ni and Ni- BaFe12O19 composite coating surfaces are shown in Figure 6. From the figure, it is evident that the barium ferrite particles are uniformly distributed throughout the Ni matrix (Figure 6(c)), and with the incorporation of the particles, there is a change in the shape of the nickel grains.
The energy dispersive X-ray analysis (EDAX) spectra recorded on the surface of the coatings confirmed the incorporation of barium hexaferrite particles in the coating (Figure 7). The weight percentage of Ni, Fe, Ba, and O were 31.71, 18.28, 9.41, and 40.59%, respectively, on a particular spot where white particles were seen.
The nanohardness values obtained from Oliver Pharr method on the cross-sections of the electrodeposited (1.55 A dm−2) Ni and Ni-BaFe12O19 coating surface were and , respectively. The improved hardness may be attributed to the dispersion strengthening of the Ni matrix due to the incorporation of barium hexaferrite particles.
The Tafel plots obtained for Ni and Ni-BaFe12O19 coatings in 3.5 wt% NaCl are shown in Figure 8. The corrosion potential (), corrosion current (), and polarization resistance () obtained from the Tafel plots are listed in Table 1. From the Tafel plots, it is clear that Ni-BaFe12O19 coating shows nobler behavior compared to plain Ni coating. Corrosion potential and corrosion current are lower for Ni-BaFe12O19 compared to Ni. This shows that, by incorporating BaFe12O19 particles in Ni matrix, the corrosion resistance of Ni can be enhanced (Table 1).
The Nyquist impedance plots for Ni and Ni-BaFe12O19 obtained in free-air (nonaerated) condition in 3.5% NaCl solution are shown in Figure 9. At higher frequencies, interception with the real axis is ascribed to the electrolyte bulk resistance (), and at low frequencies an interphase appears whose interception with the real axis is ascribed to the charge transfer resistance (). In case of Ni-BaFe12O19, additional Warburg diffusion behavior was observed at low frequency region, which represents a kind of resistance to mass transfer. A Warburg diffusional phenomenon, which suggests diffusion-controlled mechanism in the corrosion reaction, was observed in the low frequency region for Ni-BaFe12O19 coating. The Warburg impedance is usually observed at low frequencies in electrochemical experiments due to the concentration polarization induced by a sluggish diffusion process . The Warburg impedance can occur due to the following two reasons: (i) if there is some porosity/cracks in the coating the electrolyte can enter through the pores and attack the substrate, and in turn the corrosion products can block the pores and further offer resistance to the electrolyte; (ii) some loosely held particles may be dislodged in the electrolyte, and thereby exposing the substrate to the electrolyte. However, cracks and pores were not seen in the FESEM images of as-prepared coating surface.
The Bode plot of Ni showed a distinct single peak corresponding to the electrode/electrolyte interface compared to Ni-BaFe12O19 (Figure 10). In both equivalent circuits, the double layer capacitance is represented by a constant phase element (), which accounts for the deviation from the ideal dielectric behavior of the nonideal capacitor. The value of Ni was about 7 kΩcm−2, and for Ni-BaFe12O19 it was 1081 kΩcm−2. It is gratifying to note that there is a good correlation between the and values. This shows that the corrosion resistance of Ni-BaFe12O19 is higher than that plain Ni. The higher value of Ni-BaFe12O19 indicates that the active area available for the corrosion attack is less when compared to Ni.
The phase angle versus log (frequency) shows that phase angle of both Ni and Ni-BaFe12O19 coatings was less than indicating their lower capacitive behavior. The value for Ni coating was higher than that of Ni-BaFe12O19 which indicates a higher capacitive behavior. The corrosion rates as calculated from (3) were and g/h, respectively, for Ni and Ni-BaFe12O19 composite coatings.
The equivalent circuit shown in Figure 11(a) was used to fit the parameters of plain Ni, and the fitted values are tabulated in Table 2. The appropriate equivalent circuit was used for fitting the parameters of Ni-BaFe12O19, and the acquired data are shown in Figure 11(b).
Barium hexaferrite particles having magnetic property prepared by the solution combustion method were incorporated in the Ni-metal matrix. The bath loading beyond 5 g/L was not possible due to the very fine nature of the combustion synthesized powder. It was gratifying to note that the anticorrosion properties of the Ni matrix could be further improved by the incorporation of hard BaFe12O19 particles in the Ni matrix. Corrosion potential and corrosion current were lower for Ni-BaFe12O19 when compared to Ni. There was an increase in the nanohardness of the Ni-composite coating with the incorporation of BaFe12O19 particles. The value of Ni was about 7 kΩcm−2, and for Ni-BaFe12O19 it was 1081 kΩcm−2. This shows that the incorporation of barium hexaferrite particles enhances the corrosion resistance of Ni-BaFe12O19 coating.
The authors thank the Director of CSIR-NAL for his encouragement and SIP-SED-02 project for the funding. The authors thank Mr. Siju and Mr. Praveen for the FESEM and nanohardness measurements.
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