Y. Hea,
S. C. Wang*a,
F. C. Walsha,
W. S. Lib,
L. Heb and
P. A. S. Reedc
aNational Centre for Advanced Tribology at Southampton (nCATS), University of Southampton, SO17 1BJ, UK. E-mail: wangs@soton.ac.uk; Tel: +44 (0)2380594638
bState Key Laboratory of Advanced Nonferrous Materials, Lanzhou University of Technology, Lanzhou 730050, China
cEngineering Materials and Surface Engineering, University of Southampton, SO17 1BJ, UK
First published on 5th May 2015
The monitoring of coating health is crucial for the assessment of wear life in service. Electrodeposition is one of most common methods used for producing coatings including composite layers by electrophoretic deposition of particles into a growing metal electrodeposit. A new luminescent Ni coating containing an embedded, blue-emitting rare-earth mixed metal oxide (BaMgAl11O17:Eu2+) phosphor has been electrodeposited successfully from an aqueous electrolyte. Two types of surfactants were utilised to study the effective co-deposition of these particles into the nickel matrix. The surfactants of non-ionic PEG (polyethylene glycol) and cationic CTAB (cetyl trimethylammonium bromide) were observed to increase the particle content in the deposit from zero to 4.6% and 11.5%, respectively. A mixture of these two surfactants produced the highest particle embedded coverage (15.6%). The feasibility of luminescent layers in monitoring the wear of coatings has also been verified in the final part of the manuscript.
Use of luminescence in coatings was first proposed in 2004.1 Physical vapour deposition (PVD) was first used to sputter a phosphorescent/fluorescent film which emitted a constant glow under an ultraviolet (UV) light. Erbium- and samarium-doped yttria stabilized zirconia layers, for example, were deposited in thermal barrier coatings.2–4 The disadvantage of this method is its reliance on expensive and less flexible facilities with limited deposition rates. In addition, the produced film is in general too thin to be used as coating protection in wider engineering applications.
Aqueous deposition, instead of non-aqueous deposition, achieves a reasonable balance between cost and performance. Electroless deposition and electrodeposition are two classical approaches. The former has an advantage over non-line-of-sight coatings but suffers from unstable solutions as well as a slow rate process with a maximum thickness of a few microns, which again limits its applications. In contrast, electrodeposition has a much faster deposition rate and allows better control of the deposition process. It is one of most successful methods for producing composite layers by electrophoretic deposition of particles into a growing metal electrodeposit,5–7 despite the challenges including the dispersion of the particles in the bath and particle adhesion ability to electrode surface. The thickness can be well controlled from a few nanometres to several hundred micrometres.8 A review of the literature, however, reveals few successful instances of preparation of luminescent coatings by aqueous deposition. One limited report is on electrolessly deposited luminescent nickel coating.9–11 The second case is electrodeposited nickel and rare-earth phosphors using an ionic liquid bath of dimethylsulfone and NiCl2.12 The plating was carried out at a temperature of 130 °C which would limit potential industry applications as such a high bath temperature is unfavourable. Furthermore, ionic liquids are expensive to scale up and can involve supply, handling and disposal problems, making their use generally unattractive to industry.
The present research aims to develop a Ni coating embedded with phosphorescent particles (BaMgAl11O17:Eu2+, BAM) which are used to detect the wear condition of coatings simply using an ultraviolet light. The challenge for electrodeposition in an aqueous solution is that the rare earth phosphors (metal oxides) are usually micron size, which are difficult to attach to the electrode surface.13 Two types of surfactants – cationic (cetyltrimethylammonium bromide, CTAB) and non-ionic (polyethylene glycol, PEG) were studied for enhancement of particle deposition. The particle concentrations were also investigated by steady-state and time-resolved luminescence spectroscopy to optimise the emission intensities.
An AISI 1002 mild steel plate was chosen for the electrodeposition substrate. Prior to deposition, the substrate was ground with 800 grit SiC paper followed by water flushing. The substrate was immersed into 10% HCl for 10 s, then rinsed by distilled water. A pure nickel plate was used as the anode. The electrodeposition was performed with magnetic stirring (5 mm diameter, 15 mm long, PTFE-coated magnetic stirrer) at 45 ± 2 °C and a current density of 4 A dm−2 for 45 min to produce a coating thickness of 19–35 μm.
Linear sweep voltammetry (LSV) measurements were performed by an Autolab PGSTA30 system to determine a suitable potential range for deposition. The working electrode was a 3 mm thick mild steel plate of dimensions 10 mm × 40 mm. The counter electrode was a platinum mesh electrode having the same overall dimensions. A saturated calomel electrode (SCE) was used for the reference electrode. Measurements were carried out using a conventional, three-electrode cell in the electrolytic bath at a linear potential scan rate of 10 mV s−1 over a potential range of 0 to −1.2 V vs. SCE.
The morphology of the BAM particles and the composite coatings was observed using a scanning electron microscope (SEM) JEOL JSM-6500F at the Engineering Electron Microscopy Centre, Southampton University. The elemental analysis was carried by Oxford energy dispersive spectrometry (EDS). The area coverage of particles in the coating and particle size distribution were evaluated using ImageJ image processing software based on the SEM backscattered electron images (BEI). Photoluminescence excitation and emission spectra were acquired at λem = 450 nm and λex = 330 nm by visible-UV/fluorescence spectrometers (slitex = 5 nm, slitem = 5 nm). The hardness of composite coatings was carried out using a Vickers' microhardness instrument at an applied load of 100 g for 15 s, with five measurements on each sample.
A reciprocating TE-77 tribometer (Phoenix, UK) was used to evaluate the friction behaviour in laboratory air with a relative humidity of 40–50% at 25 °C. The counter body was an AISI-52100 stainless steel ball (diameter 6 mm) with a hardness of 700 HV. The studies were carried out (avoiding coating failure) on a load of 14 N with an initial Hertzian contact pressure of 0.31 GPa, a sliding frequency of 1 Hz and a sliding stroke of 2.69 mm. The total sliding times were 30 min and 90 min respectively for the Ni/BAM coating and double layer coating system (Ni + Ni/BAM). The wear track was analysed by both Alicona infinite focus optical microscopy and fluorescent microscopy.
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Fig. 1 Schematic diagrams showing luminescent particles codeposited as top layer in (a) or interlayer in (b), and the coating appearance in the damaged area. |
With the addition of PEG, the potential shifted significantly toward negative values at a given current density. At a current density of 4 A dm−2, the potentials were −1.1 V and −1.3 V for the coatings from the baths without surfactant and with PEG addition. The high negative overpotential accompanied by intensive hydrogen evolution, caused a number of pores and eventually affected coating quality. As a result, PEG was not considered as a sole surfactant. In contrast, the two coatings, produced from the baths with the addition of CTAB and PEG + CTAB, showed potentials of approximately −1.2 V at 4 A dm−2. And the mixed surfactants were more effective for the codeposition of nickel and luminescent particles.
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Fig. 4 (a) Coefficient of friction against sliding time for the Ni and Ni/BAM coatings; (b) wear rate and hardness of Ni/BAM coatings vs. BAM content in coating. |
For an inert particle in a bath to grow into the deposit involves convection, diffusion and then adsorption and reduction at the electrode surface, before such particles can be embedded in the metal.17–19 When the force of adhesion is strong enough to resist the shear force due to gravity, particles begin to be incorporated into the growing metal layer. In this study, for micron size (>1 μm) particles with a high density (>3.2 g cm−3) in the absence of a surfactant, the gravitational force appears larger than the sum of other forces, hence the majority of the particles can't attach to the electrode surface and no effective incorporation of particles can occur (Fig. 5a). Thus, without surfactant, the particles tend to settle and agglomerate at the bottom of the electrolyte.
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Fig. 5 Schematic illustration of the codeposition process of particles in electrolyte with (a) no surfactant, (b) PEG or (c) CTAB. |
PEG (Mn = 6000) is a non-ionic surfactant with a long chain structure H–(O–CH2–CH2)136–OH. With such a structure PEG is hydrophilic in water (H–OH). In the electrolyte solution, The OH− of PEG will migrate into the BAM particles and H+ will orient towards the water (Fig. 5b). The adsorbed PEG layer can provide steric separation and its hydrophilicity can inhibit the particles from merging into larger aggregates, so less sedimentation is expected. With the applied electricity, the hydrogen-bond of PEG will be attracted strongly by existing electrons in the cathode. The electronic force will hold the particles on the electrode surface longer and this enhances the incorporation of particles into the metal matrix.
CTAB molecule, (C16H33)N(CH3)3Br, is a long chain cationic surfactant. It consists of a hydrophobic tail and a non-charged hydrophilic head (as shown in Fig. 5c): the former part preferentially adsorbs on particles, whereas the latter part keeps away from the particles.20,21 This electrostatic repulsion helps to produce a stable dispersion in the electrolyte. As a cationic surfactant, CTAB can not only improve the stability of particle suspension but also charge the non-conductive particles positively via electrostatic adsorption.22 Therefore, the cationic particles will be attracted strongly to the cathode surface under the applied potential. This helps explain why the particle area coverage with CTAB was 6.9% higher than that with PEG.
With the addition of both PEG and CTAB, the area coverage of BAM particles was 15.6% which is almost the sum of the sole surfactant effects. It indicates the additive effect of CTAB and PEG operating on the particle surface, so the embedding of ceramic particles can be maximised by the suspension enhanced by PEG and the increase of the adhesion force between the cationic particles and the cathode by CTAB.
The non-ionic surfactant PEG and the cationic surfactant CTAB have different effects on the electrodeposition reaction, as indicated in the LSV curves of Fig. 3. The adsorption of the PEG onto the electrode surface took up some available sites and made charge transfer unavailable at these sites,23 the resistance will increase and accordingly the voltage i.e. overpotential. A high negative overpotential usually results in intensive hydrogen evolution which may block the deposition of particles and Ni ions. The situation is quite different for CTAB, as it is an active cationic surfactant.24 If the applied deposition potential becomes more negative than its reduction potential, the CTAB molecule (with or without BAM connected) on the electrode will be reduced and the CTAB in solution will diffuse toward the cathode surface, which compensates the curve shift in Fig. 3. As a consequence, it is more effective in enhancing the deposition of particles and a higher percentage of BAM can be achieved during the composite electrodeposition process.
With the addition of the two surfactants, the LSV of Ni/BAM electrodeposition is similar to that from a bath containing CTAB in Fig. 3. This may indicate that the individual particle is covered by a mixture of CTAB and PEG. It also explains why the particle area coverage is close to the sum of those by achieved individually by CTAB and PEG additions. The anionic/non-ionic surfactant combination has been reported to improve the embedment of particles in other composite plating systems such as Ni/PTFE (polytetrafluoroethylene polymer composite), Ni–P/PTFE or Ni–TiO2–SiO2.25–27
Having demonstrated the principle of wear detection via embedded luminescent particles in a composite metal–ceramic particle electrodeposit, it should be possible to extend the technique in several ways for monitoring of surfaces undergoing coating wear, damage or removal. For example, (a) partial removal of a coating due to wear might be followed by continuous reduction of phosphorescent intensity, (b) a multi-layered coating with different coloured phosphors in successive, controlled thickness layers could be used or (c) a continuously changing phosphor level in a compositionally modulated coating could be used to produce a phosphorescent signal which is depth sensitive.
A long-term goal of this work is to develop a sensing system based on coatings in order to monitor deterioration during service. The damage has been analysed here using infinite focus optical microscopy and fluorescent microscopy under laboratory conditions. Recently introduced UV fluorescent probes can be used for accurate on-site monitoring. Such probes can be lightweight, compact, and handheld, hence suitable for field application.
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