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ELECTRODEPOSITED NI-BASED 
NANOCOMPOSITES
ELECTRODEPOSITION 
ā€¢ Electroplating is often also called "electrodepositionā€œ. 
ā€¢ Itā€™s a process using electrical current to reduce cations of a desired 
material from a solution and coat that material as a thin film onto a 
conductive substrate surface. 
ā€¢ The overall process is also known as electrolysis.
OBJECTIVE 
ā€¢ To apply thin films of material to the surface of an object to change 
its external properties such as to increase corrosion protection, 
increase abrasion resistance, improve decorative quality or simply to 
deposit a layer which is part of a more complicated device. 
ā€¢ MECHANICAL PROPERTIES: Mechanical properties of the 
electrodeposited film depend to a considerable extent on the types 
and amounts of growth-inhibiting substance at the cathode surfaces. 
ā€¢ ADHESION: It is desirable that the substrate and the deposited 
metal interdiffuse with interlocking grains to give a continuous 
interfacial region.
APPLICATIONS 
ā€¢ Decoration: Coating a more expensive metal onto a base metal 
surface in order to improve the appearance. Applications are 
jewellery , furniture fittings, buildersā€™ hardware and tableware. 
ā€¢ Protection: Corrosion-resistant coatings such as chromium plating of 
automobile parts and domestic appliances, zinc and cadmium 
plating of nuts, screws and electrical components. Wear-resistant 
coatings such as nickel or chromium plating of bearing surfaces and 
worn shafts and journals. 
ā€¢ Electroforming: Manufacture of sieves, screens, dry shaver heads, 
record stampers, moulds, and dies. 
ā€¢ Enhancement: coatings with improved electrical and thermal 
conductivity, solderability, reflectivity etc.
ā€¢ nano-composite coatings can give various properties, such as wear 
resistance, high-temperature corrosion protection, oxidation 
resistance and self-lubrication, to a plated surface. 
ā€¢ Research on electrodeposition of nano-composite coatings has 
been attention directed towards the determination of optimum 
conditions for their production, i.e. current density, temperature, 
particle concentration and bath composition.
ELECTRODEPOSITION OF NIā€“SIC NANO-COMPOSITE 
COATINGS 
ā€¢ EXPERIMENTAL DETAILS:- 
ā€¢ Cathodes, made of copper were positioned in vertical plane with 
anode. A platinum plate was used as the anode. 
ā€¢ Analytical reagents and distilled water were used to prepare the 
plating solution. Prior to plating, the SiC nano-particulates of a mean 
diameter 50 nm with concentration of 1ā€“20 g Lāˆ’1 were dispersed in 
the electrolyte in the presence of saccharine.
ā€¢ Niā€“SiC composites have been commercialized for the protection of 
friction parts, combustion engines and casting moulds. 
ā€¢ The effects of the incorporated SiC on the cathodic efficiency of 
bath, corrosion and wear resistance of the nanocomposite coatings 
were analyzed. 
ā€¢ The dependence of SiC nano-particulates amount in the nano-composite 
coatings was investigated in relation to the SiC 
concentration in bath, cathode current density, stir rate and 
temperature of plating bath and it is shown that these parameters 
strongly affected the volume percentage of SiC nano-particulates.
ā€¢ This can be attributed to 
polarization at surface of 
cathode with increasing 
current density 
and temperature.
ā€¢ When the SiC nano-particulates 
collide at the 
cathode surface, the conditions 
for deposit formation are 
established and so the 
cathode efficiency increases.
ā€¢ where a higher particle 
concentration in the electrolyte 
increases the adsorption, thus 
resulting in a higher weight 
percent of SiC nano-particulates in 
composite coatings, while the 
decrease in the weight percent of 
the SiC nano-particulates at a 
concentration of SiC 
nanoparticulates above 5 g/ L is 
attributed to the agglomeration of 
the SiC nano-particulates in the 
electrolyte owing to their poor 
wettability.
ā€¢ Increasing the stirring rate up to 120 rpm causes to increase the 
percent of SiC nano-particulates but when the stirring rate is too 
high, the decreasing trend of the weight percent is principally caused 
by the collision factor. At a high-stirring rate, because of turbulent 
flow in bath, the SiC nano-particulates on the cathode surface are 
washed away and thus the SiC nanoparticulates percent in 
composite coating decreases.
ā€¢ Before the maximum the increasing 
percent of SiC nano-particulates can 
be attributed to the increasing 
tendency for adsorbed particles to 
arrive in the cathode surface.The 
process is controlled by the 
adsorption of the particles and the 
particle deposition is dominant. 
ā€¢ When current density is greater than 
20 mA/cm2, the decreasing trend 
can be explained by the fact that an 
increase in current density results in 
more rapid deposition of the metal 
matrix and fewer particles are 
embedded in the coating. Hence, 
the metal deposition dominates the 
deposition process.
ā€¢ Below 50 ā—¦C, the activity of 
particulates increases with 
increasing the temperature of 
bath. However, as the temperature 
of bath is higher than 50 ā—¦C, the 
thermodynamic movement of the 
ions is greatly enhanced, which 
results in increasing the kinetic 
energy of particulates. increasing 
the temperature leads to the 
decrease in the adsorpability of 
the particulates and hence to 
decrease the overpotential of the 
cathode and the electric field, 
which makes it harder for the 
particulates to be embedded in the 
matrix and subsequently leads to 
a decrease in the weight percent 
of the SiC nano-particulates in the 
composite coating.
SEM morphology of 
nickel coating. 
SEM morphology of 
Niā€“SiC nano-composite 
coating.
ā€¢ The figure reveals that the pure nickel deposit has exhibited 
irregular polyhedral crystals. The incorporation of SiC nano-particulates 
has modified the surface to particulate like 
crystals. The change in the morphology can be associated to 
the change from preferred orientation to random oriented 
composite deposits. 
ā€¢ EDX analysis revealed the uniform distribution of SiC in the 
composite. In addition, many nodular agglomerated grains are 
seen on the nano-composite coating surface (Fig. 7c). 
ā€¢ It is supposed that the SiC nano-particulates of a uniform 
distribution and agglomeration to some extent may contribute 
to increase the wear resistance of the Niā€“SiC nano-composite 
coating.
ā€¢ Fig. shows the variation in the microhardness and wear rate of the 
Niā€“SiC nano-composite coatings with the content of SiC nano-particulates. 
It is seen that the Niā€“5% SiC nano-composite coating 
has a maximum hardness and minimum wear rate. 
ā€¢ The microhardness of the nano-composite coatings increases with 
increasing weight percent of the SiC nano-particulate.Since the SiC 
nano-particulates deposited in the nickel matrix could restrain the 
growth of the nickel grains and the plastic deformation of the matrix 
under a loading, by way of grain fining and dispersive strengthening 
effects. The grain fining and dispersive strengthening effects 
become stronger with increasing SiC nano-particulates content, thus 
the microhardness and wear resistance of the Niā€“SiC nano-composite 
coatings increase with increasing SiC nanoparticulates 
content.
Electrodeposition and mechanical properties of Niā€“carbon 
nanotube nanocomposite coatings 
ā€¢ EXPERIMENTAL PROCEDURE 
ā€¢ Niā€“CNT nanocomposite coatings were electrodeposited in a sulfate 
Watts bath of the following composition: 260 g/L nickel sulfate 
(NiSO4 6H2O), 45 g/L nickel chloride (NiCl2 6H2O), 15 g/L boric 
acid (H3BO3), and 0.5 g/L saccharine. To improve MWCNT 
dispersion, SDS and HPC were added into the electrodeposition 
solutions by varying the amounts of SDS and HPC from 0 to 10 g/L. 
ā€¢ The total amount of SDS and HPC was always kept as10 g/L. 
MWCNTs of 10ā€“15 nm diameter, produced by CVD, were used to 
form the Niā€“CNT electrodeposition solutions. 
ā€¢ Niā€“CNT nanocomposites of 50 mm thickness were electrodeposited 
on Cu substrates of 2 cm2 cm size at a current density of 40 
mA/cm2. During electrodeposition of a Niā€“CNT nanocomposite, the 
bath was maintained at 40C with mechanical stirring at 500 rpm.
FESEM micrographs of the Niā€“CNT nanocomposite electrodeposited in a bath containing 
dispersion additive of (a) 10 g/L SDS, (b) 7.5 g/L SDS and 2.5 g/L HPC, (c) 5 g/L SDS and 5
ā€¢ Fig. 1 illustrates surface morphologies of the Niā€“CNT nanocomposites 
electrodeposited in solutions with different amounts of SDS and HPC as 
dispersion additives. The MWCNT concentration of the electrodeposition 
solutions was maintained as 10 g/L and the total amount of SDS and HPC 
was also kept as 10 g/L. Comparing Fig. 1(a) with Fig. 1(e) indicates that 
SDS is more effective for MWCNT dispersion than HPC. As shown in Fig. 
1(b) and (c), however, incorporation of MWCNTs into Ni matrix was greatly 
enhanced by using SDSā€“HPC mixture with the SDSā€“HPC weight ratios of 
3:1 and 1:1. Such SDSā€“HPC mixture might modify the surface chemistry of 
MWCNTs more suitable for uniform dispersion in the electrolytic bath, 
resulting in great increase in the MWCNT content of the Niā€“CNT 
nanocomposite. SDSā€“HPC mixture additive affected not only the MWCNT 
dispersion characteristics but also the properties of Ni matrix itself. While 
the hardness of a Ni coating electrodeposited without MWCNTs in a Watt 
bath containing SDS of 10 g/L was 430 Hv, the value of one processed in a 
solution with the SDSā€“HPC mixture of the 3:1 weight ratio increased to 527 
Hv.
FESEM micrographs of the Niā€“CNT nanocomposite electrodeposited in 
a bath containing an MWCNT concentration of (a) 1 g/L, (b) 2 g/L, (c) 
5 g/L, and (d) 10 g/L.
ā€¢ shows SEM micrographs of the Niā€“CNT nanocomposites 
processed in the electrodeposition solutions with the 
MWCNT concentrations of 0ā€“10 g/L and the 10 g/L SDSā€“ 
HPC mixture of the weight ratio of 3:1. 
ā€¢ The Niā€“CNT nanocomposites were etched in nitric acid 
to remove the surface layer for observation of the internal 
morphology. With increasing the MWCNT concentration 
in the electrodeposition bath up to 5 g/L, more MWCNTs 
were incorporated into Ni matrix. However, microstructure 
of the Niā€“CNT composite became porous with increasing 
the MWCNT concentration in the bath beyond 2 g/L.
ā€¢ The MWCNT content in the Niā€“CNT 
ā€¢ nanocomposite became larger and reached a maximum of 
ā€¢ 22.5 vol% with increasing the MWCNT concentration in 
ā€¢ the bath up to 5 g/L. However, the MWCNT content in the 
ā€¢ composite decreased with further increasing the MWCNT 
ā€¢ concentration in the bath beyond 5 g/L, which could be due 
ā€¢ to the agglomeration of MWCNTs in the bath containing 
ā€¢ MWCNTs above the saturation concentration [4]. As the 
ā€¢ MWCNT content decreased and the microstructure 
ā€¢ became substantially porous for the nanocomposite 
ā€¢ processed in the bath containing MWCNTs of 10 g/L, 
ā€¢ mechanical characterization was not conducted for this 
ā€¢ specimen.
ā€¢ With increasing the MWCNT 
content of the Niā€“CNT 
composite to 14.6 vol%, the 
fracture stress was improved 
from 607 to 780MPa. However, 
the fracture stress dropped 
drastically to 534MPa for the 
specimen with the MWCNT 
content of 22.5 vol% as 
fabricated in the bath of the 
MWCNT concentration of 5 
g/L. This might be due to the 
porous microstructure ofthe 
nanocomposite with MWCNT 
content of 22.5 vol%.
The morphology of electrodeposited pure nickel and Niā€“CeO2 nanocomposite. 
(a) Pure nickel; (b) Niā€“CeO2 nanocomposites
ā€¢ A pyramid structure as shown in Fig. 1(a) is observed at the surface 
of the pure nickel. Whereas, with the addition of CeO2 
nanoparticles, the grain size is reduced and the morphology is 
changed to the hemispherical grain structure, as shown in Fig. 1(b). 
ā€¢ In the electrocodeposition process, CeO2 particles adsorb cations in 
the bath under the high potential gradient. They will then be 
transported to the cathode surface by electrophoresis, and will be 
further adsorbed onto the cathode surface. This phenomenon 
results in: (a) an increase in electrocrystalline potential because the 
incorporated nanoparticles decrease the electrical cathode surface; 
and (b) the occurrence of new nuclei because the adsorbed 
nanoparticles limit the growth of the original crystal grains . It is 
considered that both of the factors are favorable for fine grains, and 
good surface morphology of the composite.
ā€¢ The microhardness of pure nickel 
is about 282.7 Hv. With an 
addition of 30 g/L CeO2 
nanoparticles, the microhardness 
of the deposit increased 
significantly to 446.2 Hv. 
ā€¢ The wear height loss of the 
composite was 18 micron as 
compared to 43 micron for pure 
nickel. 
ā€¢ It is known that the microstructure 
of the electrodeposit is refined 
when nanoparticles are 
embedded. It will increase the 
load carrying capacity and 
improve the resistance for plastic 
deformation.
ā€¢ shows the corrosion potential and corrosion current 
ā€¢ obtained from an immersion test with a 3.5 wt.% NaCl 
ā€¢ solution. The results indicate that the nanocomposite 
ā€¢ obtained from the bath containing 30 g l1 CeO2 nanoparticles 
ā€¢ and at the current density of 1 Adm2 exhibits the 
ā€¢ best corrosion resistance. Balathandan et al. reported that 
ā€¢ the corrosion potential and corrosion current of Ni matrix 
ā€¢ reinforced with micron CeO2 particles were 550 mV and 
ā€¢ 4 lA cm2, respectively, which are superior to Niā€“ZrO2, 
ā€¢ Niā€“PSZ, and pure Ni coatings [9]. In the present experiments, 
ā€¢ the corrosion potential and corrosion current of 
ā€¢ the nanocomposite were found to be 195.458 mV and 
ā€¢ 1.020 lA cm2, respectively, illustrating a significant 
ā€¢ improvement in corrosion resistance over the composite 
ā€¢ with micro-sized particles. It is considered that when 
ā€¢ CeO2 nanosized particles are embedded in the nickel 
ā€¢ matrix, the corrosion path is more seriously distorted as 
ā€¢ compared to micro-sized particles, which is favorable for 
ā€¢ corrosion resistance. In fact, the fine grain structure arising 
ā€¢ from the co-electrodeposition of CeO2 nanoparticles also 
ā€¢ promotes good corrosion resistance as compared to coarse 
ā€¢ grain structure [13,14].

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Electrodeposit Ni-SiC Nanocomposites

  • 2. ELECTRODEPOSITION ā€¢ Electroplating is often also called "electrodepositionā€œ. ā€¢ Itā€™s a process using electrical current to reduce cations of a desired material from a solution and coat that material as a thin film onto a conductive substrate surface. ā€¢ The overall process is also known as electrolysis.
  • 3. OBJECTIVE ā€¢ To apply thin films of material to the surface of an object to change its external properties such as to increase corrosion protection, increase abrasion resistance, improve decorative quality or simply to deposit a layer which is part of a more complicated device. ā€¢ MECHANICAL PROPERTIES: Mechanical properties of the electrodeposited film depend to a considerable extent on the types and amounts of growth-inhibiting substance at the cathode surfaces. ā€¢ ADHESION: It is desirable that the substrate and the deposited metal interdiffuse with interlocking grains to give a continuous interfacial region.
  • 4. APPLICATIONS ā€¢ Decoration: Coating a more expensive metal onto a base metal surface in order to improve the appearance. Applications are jewellery , furniture fittings, buildersā€™ hardware and tableware. ā€¢ Protection: Corrosion-resistant coatings such as chromium plating of automobile parts and domestic appliances, zinc and cadmium plating of nuts, screws and electrical components. Wear-resistant coatings such as nickel or chromium plating of bearing surfaces and worn shafts and journals. ā€¢ Electroforming: Manufacture of sieves, screens, dry shaver heads, record stampers, moulds, and dies. ā€¢ Enhancement: coatings with improved electrical and thermal conductivity, solderability, reflectivity etc.
  • 5. ā€¢ nano-composite coatings can give various properties, such as wear resistance, high-temperature corrosion protection, oxidation resistance and self-lubrication, to a plated surface. ā€¢ Research on electrodeposition of nano-composite coatings has been attention directed towards the determination of optimum conditions for their production, i.e. current density, temperature, particle concentration and bath composition.
  • 6. ELECTRODEPOSITION OF NIā€“SIC NANO-COMPOSITE COATINGS ā€¢ EXPERIMENTAL DETAILS:- ā€¢ Cathodes, made of copper were positioned in vertical plane with anode. A platinum plate was used as the anode. ā€¢ Analytical reagents and distilled water were used to prepare the plating solution. Prior to plating, the SiC nano-particulates of a mean diameter 50 nm with concentration of 1ā€“20 g Lāˆ’1 were dispersed in the electrolyte in the presence of saccharine.
  • 7. ā€¢ Niā€“SiC composites have been commercialized for the protection of friction parts, combustion engines and casting moulds. ā€¢ The effects of the incorporated SiC on the cathodic efficiency of bath, corrosion and wear resistance of the nanocomposite coatings were analyzed. ā€¢ The dependence of SiC nano-particulates amount in the nano-composite coatings was investigated in relation to the SiC concentration in bath, cathode current density, stir rate and temperature of plating bath and it is shown that these parameters strongly affected the volume percentage of SiC nano-particulates.
  • 8.
  • 9. ā€¢ This can be attributed to polarization at surface of cathode with increasing current density and temperature.
  • 10. ā€¢ When the SiC nano-particulates collide at the cathode surface, the conditions for deposit formation are established and so the cathode efficiency increases.
  • 11. ā€¢ where a higher particle concentration in the electrolyte increases the adsorption, thus resulting in a higher weight percent of SiC nano-particulates in composite coatings, while the decrease in the weight percent of the SiC nano-particulates at a concentration of SiC nanoparticulates above 5 g/ L is attributed to the agglomeration of the SiC nano-particulates in the electrolyte owing to their poor wettability.
  • 12. ā€¢ Increasing the stirring rate up to 120 rpm causes to increase the percent of SiC nano-particulates but when the stirring rate is too high, the decreasing trend of the weight percent is principally caused by the collision factor. At a high-stirring rate, because of turbulent flow in bath, the SiC nano-particulates on the cathode surface are washed away and thus the SiC nanoparticulates percent in composite coating decreases.
  • 13. ā€¢ Before the maximum the increasing percent of SiC nano-particulates can be attributed to the increasing tendency for adsorbed particles to arrive in the cathode surface.The process is controlled by the adsorption of the particles and the particle deposition is dominant. ā€¢ When current density is greater than 20 mA/cm2, the decreasing trend can be explained by the fact that an increase in current density results in more rapid deposition of the metal matrix and fewer particles are embedded in the coating. Hence, the metal deposition dominates the deposition process.
  • 14. ā€¢ Below 50 ā—¦C, the activity of particulates increases with increasing the temperature of bath. However, as the temperature of bath is higher than 50 ā—¦C, the thermodynamic movement of the ions is greatly enhanced, which results in increasing the kinetic energy of particulates. increasing the temperature leads to the decrease in the adsorpability of the particulates and hence to decrease the overpotential of the cathode and the electric field, which makes it harder for the particulates to be embedded in the matrix and subsequently leads to a decrease in the weight percent of the SiC nano-particulates in the composite coating.
  • 15. SEM morphology of nickel coating. SEM morphology of Niā€“SiC nano-composite coating.
  • 16. ā€¢ The figure reveals that the pure nickel deposit has exhibited irregular polyhedral crystals. The incorporation of SiC nano-particulates has modified the surface to particulate like crystals. The change in the morphology can be associated to the change from preferred orientation to random oriented composite deposits. ā€¢ EDX analysis revealed the uniform distribution of SiC in the composite. In addition, many nodular agglomerated grains are seen on the nano-composite coating surface (Fig. 7c). ā€¢ It is supposed that the SiC nano-particulates of a uniform distribution and agglomeration to some extent may contribute to increase the wear resistance of the Niā€“SiC nano-composite coating.
  • 17.
  • 18. ā€¢ Fig. shows the variation in the microhardness and wear rate of the Niā€“SiC nano-composite coatings with the content of SiC nano-particulates. It is seen that the Niā€“5% SiC nano-composite coating has a maximum hardness and minimum wear rate. ā€¢ The microhardness of the nano-composite coatings increases with increasing weight percent of the SiC nano-particulate.Since the SiC nano-particulates deposited in the nickel matrix could restrain the growth of the nickel grains and the plastic deformation of the matrix under a loading, by way of grain fining and dispersive strengthening effects. The grain fining and dispersive strengthening effects become stronger with increasing SiC nano-particulates content, thus the microhardness and wear resistance of the Niā€“SiC nano-composite coatings increase with increasing SiC nanoparticulates content.
  • 19. Electrodeposition and mechanical properties of Niā€“carbon nanotube nanocomposite coatings ā€¢ EXPERIMENTAL PROCEDURE ā€¢ Niā€“CNT nanocomposite coatings were electrodeposited in a sulfate Watts bath of the following composition: 260 g/L nickel sulfate (NiSO4 6H2O), 45 g/L nickel chloride (NiCl2 6H2O), 15 g/L boric acid (H3BO3), and 0.5 g/L saccharine. To improve MWCNT dispersion, SDS and HPC were added into the electrodeposition solutions by varying the amounts of SDS and HPC from 0 to 10 g/L. ā€¢ The total amount of SDS and HPC was always kept as10 g/L. MWCNTs of 10ā€“15 nm diameter, produced by CVD, were used to form the Niā€“CNT electrodeposition solutions. ā€¢ Niā€“CNT nanocomposites of 50 mm thickness were electrodeposited on Cu substrates of 2 cm2 cm size at a current density of 40 mA/cm2. During electrodeposition of a Niā€“CNT nanocomposite, the bath was maintained at 40C with mechanical stirring at 500 rpm.
  • 20. FESEM micrographs of the Niā€“CNT nanocomposite electrodeposited in a bath containing dispersion additive of (a) 10 g/L SDS, (b) 7.5 g/L SDS and 2.5 g/L HPC, (c) 5 g/L SDS and 5
  • 21. ā€¢ Fig. 1 illustrates surface morphologies of the Niā€“CNT nanocomposites electrodeposited in solutions with different amounts of SDS and HPC as dispersion additives. The MWCNT concentration of the electrodeposition solutions was maintained as 10 g/L and the total amount of SDS and HPC was also kept as 10 g/L. Comparing Fig. 1(a) with Fig. 1(e) indicates that SDS is more effective for MWCNT dispersion than HPC. As shown in Fig. 1(b) and (c), however, incorporation of MWCNTs into Ni matrix was greatly enhanced by using SDSā€“HPC mixture with the SDSā€“HPC weight ratios of 3:1 and 1:1. Such SDSā€“HPC mixture might modify the surface chemistry of MWCNTs more suitable for uniform dispersion in the electrolytic bath, resulting in great increase in the MWCNT content of the Niā€“CNT nanocomposite. SDSā€“HPC mixture additive affected not only the MWCNT dispersion characteristics but also the properties of Ni matrix itself. While the hardness of a Ni coating electrodeposited without MWCNTs in a Watt bath containing SDS of 10 g/L was 430 Hv, the value of one processed in a solution with the SDSā€“HPC mixture of the 3:1 weight ratio increased to 527 Hv.
  • 22. FESEM micrographs of the Niā€“CNT nanocomposite electrodeposited in a bath containing an MWCNT concentration of (a) 1 g/L, (b) 2 g/L, (c) 5 g/L, and (d) 10 g/L.
  • 23. ā€¢ shows SEM micrographs of the Niā€“CNT nanocomposites processed in the electrodeposition solutions with the MWCNT concentrations of 0ā€“10 g/L and the 10 g/L SDSā€“ HPC mixture of the weight ratio of 3:1. ā€¢ The Niā€“CNT nanocomposites were etched in nitric acid to remove the surface layer for observation of the internal morphology. With increasing the MWCNT concentration in the electrodeposition bath up to 5 g/L, more MWCNTs were incorporated into Ni matrix. However, microstructure of the Niā€“CNT composite became porous with increasing the MWCNT concentration in the bath beyond 2 g/L.
  • 24.
  • 25. ā€¢ The MWCNT content in the Niā€“CNT ā€¢ nanocomposite became larger and reached a maximum of ā€¢ 22.5 vol% with increasing the MWCNT concentration in ā€¢ the bath up to 5 g/L. However, the MWCNT content in the ā€¢ composite decreased with further increasing the MWCNT ā€¢ concentration in the bath beyond 5 g/L, which could be due ā€¢ to the agglomeration of MWCNTs in the bath containing ā€¢ MWCNTs above the saturation concentration [4]. As the ā€¢ MWCNT content decreased and the microstructure ā€¢ became substantially porous for the nanocomposite ā€¢ processed in the bath containing MWCNTs of 10 g/L, ā€¢ mechanical characterization was not conducted for this ā€¢ specimen.
  • 26. ā€¢ With increasing the MWCNT content of the Niā€“CNT composite to 14.6 vol%, the fracture stress was improved from 607 to 780MPa. However, the fracture stress dropped drastically to 534MPa for the specimen with the MWCNT content of 22.5 vol% as fabricated in the bath of the MWCNT concentration of 5 g/L. This might be due to the porous microstructure ofthe nanocomposite with MWCNT content of 22.5 vol%.
  • 27. The morphology of electrodeposited pure nickel and Niā€“CeO2 nanocomposite. (a) Pure nickel; (b) Niā€“CeO2 nanocomposites
  • 28. ā€¢ A pyramid structure as shown in Fig. 1(a) is observed at the surface of the pure nickel. Whereas, with the addition of CeO2 nanoparticles, the grain size is reduced and the morphology is changed to the hemispherical grain structure, as shown in Fig. 1(b). ā€¢ In the electrocodeposition process, CeO2 particles adsorb cations in the bath under the high potential gradient. They will then be transported to the cathode surface by electrophoresis, and will be further adsorbed onto the cathode surface. This phenomenon results in: (a) an increase in electrocrystalline potential because the incorporated nanoparticles decrease the electrical cathode surface; and (b) the occurrence of new nuclei because the adsorbed nanoparticles limit the growth of the original crystal grains . It is considered that both of the factors are favorable for fine grains, and good surface morphology of the composite.
  • 29. ā€¢ The microhardness of pure nickel is about 282.7 Hv. With an addition of 30 g/L CeO2 nanoparticles, the microhardness of the deposit increased significantly to 446.2 Hv. ā€¢ The wear height loss of the composite was 18 micron as compared to 43 micron for pure nickel. ā€¢ It is known that the microstructure of the electrodeposit is refined when nanoparticles are embedded. It will increase the load carrying capacity and improve the resistance for plastic deformation.
  • 30.
  • 31. ā€¢ shows the corrosion potential and corrosion current ā€¢ obtained from an immersion test with a 3.5 wt.% NaCl ā€¢ solution. The results indicate that the nanocomposite ā€¢ obtained from the bath containing 30 g l1 CeO2 nanoparticles ā€¢ and at the current density of 1 Adm2 exhibits the ā€¢ best corrosion resistance. Balathandan et al. reported that ā€¢ the corrosion potential and corrosion current of Ni matrix ā€¢ reinforced with micron CeO2 particles were 550 mV and ā€¢ 4 lA cm2, respectively, which are superior to Niā€“ZrO2, ā€¢ Niā€“PSZ, and pure Ni coatings [9]. In the present experiments, ā€¢ the corrosion potential and corrosion current of ā€¢ the nanocomposite were found to be 195.458 mV and ā€¢ 1.020 lA cm2, respectively, illustrating a significant ā€¢ improvement in corrosion resistance over the composite ā€¢ with micro-sized particles. It is considered that when ā€¢ CeO2 nanosized particles are embedded in the nickel ā€¢ matrix, the corrosion path is more seriously distorted as ā€¢ compared to micro-sized particles, which is favorable for ā€¢ corrosion resistance. In fact, the fine grain structure arising ā€¢ from the co-electrodeposition of CeO2 nanoparticles also ā€¢ promotes good corrosion resistance as compared to coarse ā€¢ grain structure [13,14].