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<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong><br />

System: Ni-electroless and Termosil ®<br />

by<br />

Gregory Demyashev, IRIS<br />

Dr. Alexander Taube, IRIS<br />

Abstract<br />

The aim <strong>of</strong> this R&D is to develop duplex coatings that are suitable for automotive<br />

applications. A topcoat <strong>of</strong> Termosil ® as the second layer <strong>of</strong> a duplex system <strong>with</strong> Nielectroless<br />

as the primary layer has allowed increased corrosion resistance <strong>of</strong> Nielectroless<br />

from 7 hours to 552 hours <strong>with</strong>out formation <strong>of</strong> red rust (RR). This<br />

significant increase in corrosion resistance does not result in increased cost <strong>of</strong> the<br />

duplex coating system in comparison <strong>with</strong> Ni-electroless plating.<br />

1. Introduction<br />

<strong>Corrosion</strong> resistance limitations <strong>of</strong> one-component coatings can be overcome by<br />

combining multi-layer coating systems. It is possible to produce a complex finish <strong>with</strong><br />

increased corrosion resistance (Dong H. et al., 1997; Fazio C. et al., 1998; Chang, S.,<br />

1985) and low coefficient <strong>of</strong> friction. In the simplest case, a multi-layer coating system<br />

consists <strong>of</strong> two different layers. Double-layer (or duplex) coating systems are defined<br />

as two finishes used in conjunction in order to create superior properties for a combined<br />

finish (Bodycote, 1998). The secondary layer is practical to preliminary treated/coated<br />

steel surface <strong>with</strong> sherardising, mechanical plating, electroplating, etc. A second layer<br />

can be applied by means <strong>of</strong> immersion and following topcoat curing.<br />

Surface engineering becomes simpler if wear-resistant and corrosion-resistant<br />

properties <strong>of</strong> coatings are separated by use <strong>of</strong> two different technologies consecutively<br />

for obtaining a duplex coating system exhibiting both corrosion and wear resistance.<br />

The technologies are subjected to process-oriented optimization <strong>of</strong> duplex coatings for<br />

corrosion/wear protection <strong>of</strong> steels.<br />

Architecture <strong>of</strong> duplex coating systems possessing both corrosion and wear<br />

protection can be realised as following:<br />

• Primary layer – usually expensive wear-resistant coatings, e.g. Ni-electroless,<br />

TiN, etc, having poor corrosion protection (Korhonen A.S. 1994; Drees D. et al.<br />

1994; Erdemir A. et al. 1985; Motojima S. & Kohno M. 1986)<br />

• Secondary layer – usually an inexpensive finish possessing high corrosion<br />

resistance and low coefficient <strong>of</strong> friction, such as Termosil, Dacromet,<br />

Dorrltech, etc, but having low hardness and wear resistance.<br />

<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong> System:<br />

Ni-electroless and Termosil<br />

1


Such duplex coatings can achieve significant corrosion resistance combined <strong>with</strong> high<br />

hardness and low friction. In short, a secondary layer can drastically improve corrosion<br />

resistance and lubricity <strong>of</strong> a steel surface <strong>with</strong>out increasing the cost <strong>of</strong> the duplex<br />

coating significantly.<br />

Termosil ® (Termosil Asia Sdn Bnd 1997) is a similar solution to Dacromet ® –<br />

A/B (Metal <strong>Coating</strong> International Inc. 1998; Ridder J.A. 1995). Termosil is a waterbased<br />

solution <strong>with</strong> dispersed Zn- and Al-flakes, proprietary organic, Cr 6+ , which is<br />

reduced to Cr 3+ into the sinter oven at ~300 0 C. Small additions <strong>of</strong> inorganic<br />

components and metal oxides are present in Termosil (White R.W. 1995). After<br />

sintering, Termosil-coatings provide outstanding corrosion protection for ferrous<br />

materials (1,000-1,200 hrs under salt spray test <strong>with</strong>out formation <strong>of</strong> red rust in<br />

comparison <strong>with</strong> 500 hrs for Dacromet), good bimetallic corrosion resistance for Al,<br />

high electrical conductivity (electrical resistance – 0.6 ), and low coefficient <strong>of</strong><br />

friction (0.09-0.1 <strong>with</strong> special lubrication agent on the top).<br />

Termosil passivating property is realized by the addition <strong>of</strong> metal oxides, which<br />

slow down corrosion reactions <strong>of</strong> zinc on steel. Damaged areas in the Termosil coating<br />

repair themselves by filling <strong>with</strong> Zinc oxides and carbonates. The final coating contains<br />

no Cr 6+ chemicals. The Zn-flakes stratify well forming a metallic sacrificial coating<br />

<strong>with</strong> Al-flakes and metal oxide dispersant.<br />

However, Termosil’s appearance is inferior to Dacromet in two respects. These<br />

are that Termosil scuffs more easily and is not available in as many colours as<br />

Dacromet. It is thought that Termosil’s excellent corrosion resistance may be due to the<br />

inclusion <strong>of</strong> 15% Al in the coating composition, which reduces corrosion rate due to the<br />

impermeability <strong>of</strong> alumina to oxygen.<br />

For selection a primary layer for duplex coatings, Ni-electroless was chosen as<br />

expensive coating having good hardness and wear resistance, but not satisfying<br />

corrosion resistance requirements by virtue <strong>of</strong> its inherent porosity (Gawrilow G.G.<br />

1979). Red rust on the AISI-52100 steel surface coated <strong>with</strong> Ni-electroless appears<br />

after 7 hours under salt spray test. The frictional coefficient <strong>of</strong> Ni-electroless is also<br />

unsatisfactory (µ NiP =0.38-0.45) for sliding steel joints.<br />

It would be very useful to develop the duplex system <strong>of</strong> Termosil for NiPelectroless<br />

as a primary layer in order to enhance corrosion resistance <strong>of</strong> NiP-Termosil<br />

system on steels. The aim <strong>of</strong> this research and development is to improve corrosion<br />

resistance <strong>of</strong> AISI-52100 (high carbon steel) coated <strong>with</strong> NiP-electroless coatings,<br />

which is used in the automotive industry, fastener manufacturing, etc, applying<br />

Termosil as the topcoat.<br />

2. Experimental procedure and corrosion testing<br />

<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong> System:<br />

Ni-electroless and Termosil<br />

2


<strong>Steel</strong> surfaces that have to be plated <strong>with</strong> Termosil must be clean, rust free, and<br />

in grease free condition. The steel surface was cleaned <strong>with</strong> solution approximately 1<br />

liter <strong>of</strong> water and 1 ml activator for 10 minutes.<br />

Industrial procedure was used for application <strong>of</strong> Termosil coatings<br />

(International Standard Organisation 1993). Termosil coatings were applied on steel<br />

surfaces <strong>with</strong> preliminary Ni-electroless coating. After centrifuging, such coated<br />

samples were pre-dried by hot air. Further, the raw Termosil coating over Ni-electroless<br />

was cured <strong>with</strong>in range <strong>of</strong> +200 0 C and +470 0 C. The heat treatment is necessary to<br />

reduce hazardous hexavalent chromium content to safe trivalent chromium system.<br />

This trivalent chromium fills out the main gaps between flakes, increasing the<br />

resistance <strong>of</strong> moisture and oxidants penetration.<br />

Such prepared samples were ready for a testing. Neutral Salt Spray Test (NSST)<br />

was chosen as a method for testing <strong>of</strong> corrosion resistance <strong>of</strong> the samples. The NSST is<br />

described elsewhere (Baboian R. 1997; ASTM 1986; ASTM 1987) and widely used in<br />

the fastener and automotive industry (Crotty D. 1996) for evaluating <strong>of</strong> corrosion<br />

resistance.<br />

The salt spray apparatus represents an environmentally controlled chamber<br />

containing a salt fog (100% humidity) <strong>of</strong> solution <strong>of</strong> 5±1 wt % NaCl <strong>with</strong> not more than<br />

0.3% <strong>of</strong> total impurities in distilled water at a temperature held at 45±2 0 C. The size and<br />

detailed construction <strong>of</strong> the apparatus provide the conditions for this method (ASTM<br />

1986). Sea water is a saline 3.4%-solution <strong>of</strong> sodium chloride (NaCl) and magnesium<br />

chloride (MgCl), and is slightly alkaline (pH 8). There are many other solution<br />

minerals, which are present in very small quantities. 5%-solution <strong>of</strong> NaCl, which has<br />

maximum corrosive ability compared to higher/lower NaCl-concentrations, is<br />

considered equivalent to sea water.<br />

3. Results and discussion<br />

At the first stage, it was important to find out the correct composition <strong>of</strong><br />

Termosil. Atomic Emission Spectroscopy was used for the aim. Results <strong>of</strong> the<br />

quantitative analysis <strong>of</strong> Termosil have been presented (e.g., Figure 3.1). Termosil is<br />

composed predominantly <strong>of</strong> Zn <strong>with</strong> addition <strong>of</strong> aluminium, tin, chromium, and iron.<br />

These aluminium-filled ceramics have electrochemical potential (-0.74 V) in aerated<br />

3.4% NaCl-solution similar to cadmium-plated mild steel (-0.76 V) (Mosser M.F. &<br />

McMordie B.G. 1994). Therefore, this particular composition, like cadmium, is optimal<br />

for corrosion protection.<br />

Zn ( at %) Al (at %) Sn (at %) Cr (at %) Fe (at %)<br />

37-51 6-10 8-18 6-7 2-10<br />

Figure 3.1 – Composition <strong>of</strong> Termosil coating after sintering.<br />

<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong> System:<br />

Ni-electroless and Termosil<br />

3


The AISI-52100 steel samples were coated <strong>with</strong> a single layer <strong>of</strong> Termosil and<br />

dried at room temperature (25 0 C). These samples have shown a very low corrosion<br />

protection in salt spray test (24 hours <strong>with</strong>out formation <strong>of</strong> RR). It means that Termosil<br />

cannot be used as a raw composition <strong>with</strong>out sintering for corrosion protection.<br />

In the next stage, the samples <strong>with</strong> one-layer-Termosil dried at 25 0 C were<br />

sintered at 250 0 C, 350 0 C, 300 0 C, and 470 0 C for 15 minutes. The samples were subject<br />

to salt spray test. The results are displayed in Figure 3.2.<br />

Temperature curing => Dried (25 0 C) 250 0 C 350 0 C 470 0 C<br />

Termosil (1 layer) 18±6 42±6 42±6 210±6<br />

Figure 3.2 – <strong>Corrosion</strong> resistance (hrs <strong>with</strong>out formation <strong>of</strong> red rust) <strong>of</strong> one-layer-<br />

Termosil over the bare AISI-52100 steel followed by sintering for 15 minutes.<br />

It is clear that any chemical transformation takes place during sintering at<br />

470 0 C. This temperature is significantly higher that is recommended (Termosil Asia<br />

Sdn Bnd 1997). The curing changes initial raw composition <strong>of</strong> Termosil to the final<br />

composition, as shown in Figure 2, at 470 0 C only. <strong>Corrosion</strong> protection achieved <strong>with</strong><br />

Termosil corresponds to 210 hrs under the NSST. However, this is not as remarkable as<br />

Termosil used in combination <strong>with</strong> a fine intermediate layer <strong>of</strong> Zn-mechanically plated<br />

(Termosil Asia Sdn Bnd 1997).<br />

Application <strong>of</strong> Termosil to improve lubricity and corrosion protection as<br />

secondary layer over Ni-electroless coating was realised (e.g. Figure 3.3).<br />

Temperature curing => 470 0 C 350 0 C<br />

Ni-electroless (primary layer) +<br />

one-layer-Termosil (secondary layer) 546±6 210±6<br />

Ni-electroless (primary layer) +<br />

two-layer-Termosil (secondary layer) 498±6 210±6<br />

Figure 3.3 – <strong>Corrosion</strong> resistance (hrs <strong>with</strong>out formation <strong>of</strong> red rust) <strong>of</strong> duplex<br />

coating (Ni-electroless + Termosil) sintered at 350 0 C and 470 0 C.<br />

One- and two-layer-Termosil over Ni-electroless were sintered at 350 0 C and<br />

470 0 C. Maximum corrosion protection was achieved <strong>with</strong> one-layer-Termosil over Nielectroless.<br />

Up to 552 hrs <strong>with</strong>out red rust under salt spray test can be achieved <strong>with</strong><br />

this combination <strong>of</strong> duplex coating systems.<br />

Ni-electroless plating costs 22-28 times more than Zn-electroplating, and<br />

Termosil application costs equal to Zn-electroplating costs. Therefore, Termosil coating<br />

over Ni-electroless does not add significant cost to this duplex coating system, i.e. only<br />

<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong> System:<br />

Ni-electroless and Termosil<br />

4


3-4% <strong>of</strong> cost <strong>of</strong> Ni-electroless. However, the achievement in corrosion resistance and<br />

lubricity is significant.<br />

5. Conclusion<br />

Application <strong>of</strong> Termosil as the second layer <strong>of</strong> duplex system in the aggregate<br />

<strong>with</strong> Ni-electroless has allowed increasing corrosion resistance <strong>of</strong> Ni-electroless from 7<br />

hours until 552 hours <strong>with</strong>out formation <strong>of</strong> red rust. Termosil coating over Nielectroless<br />

increases the cost <strong>of</strong> this duplex coating system by only 3-5% <strong>of</strong> the initial<br />

cost <strong>of</strong> Ni-electroless.<br />

References<br />

ASTM 1986, ASTM Neutral Salt Spray B-117, n.p.<br />

ASTM 1987, ASTM Modified Salt Fog Testing G-85, n.p.<br />

Baboian R. 1997, CORROSION TESTS AND STANDARDS: Application and<br />

Interpretation, ASTM, New York.<br />

Bodycote Metal Technology Inc. 1998, <strong>Duplex</strong> <strong>Coating</strong> System, n.p.<br />

Chang, S. (ed.) 1985, Canning Handbook on Electroplating, Plenum Press, New York.<br />

Crotty D. 1996, “Zinc Alloy Plating for the Automotive Industry”, Metal Finishing, No.<br />

9, pp 54-58.<br />

Dong H., Sun Y. & Bell T. 1997, “Enhanced corrosion resistance <strong>of</strong> duplex coatings”,<br />

Surface and <strong>Coating</strong>s Technology, Vol. 90, pp 91-101.<br />

Drees D., Vancoille E., Celis J.P. & Roos J.R. 1994, “Structural characteristics <strong>of</strong> PVD<br />

Ti-based coatings in relation to their wear and corrosion behaviour”, Materials Science<br />

Forum, Vol. 163-165, pp 509-526.<br />

Erdemir A., Carter W.B. & Hochman R.F. 1985, “A Study <strong>of</strong> the <strong>Corrosion</strong> behaviour<br />

<strong>of</strong> TiN Films”, Materials Science and Engineering, Vol. 69, No.1, pp 89-93.<br />

Fazio C., Lanzoni E., Martini C. & Romagnoli D. 1998, “ACD-Ni/PVD-CrN duplex<br />

coatings to enhance corrosion and wear resistance”, in 11 th Congress <strong>of</strong> the<br />

International Federation for Heat Treatment and Surface Engineering, Florence, Italy,<br />

19-21 October, Vol. 3, pp 169-178.<br />

Gawrilow G.G. 1979, Chemical (Electroless) Nickel-Plating, Portcullis Press, Redhill.<br />

<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong> System:<br />

Ni-electroless and Termosil<br />

5


International Standard Organisation 1993, “Fasteners – Non-electrolytically applied<br />

zinc flake coatings”, ISO/TC-1/SC-1/WG-1, No. 66.<br />

Korhonen A.S. 1994, “<strong>Corrosion</strong> <strong>of</strong> thin hard PVD coatings”, Vacuum, Vol. 45, No.<br />

10/11, pp 1031-1034.<br />

Motojima S. & Kohno M. 1986, “<strong>Corrosion</strong> and Abrasion Resistivities to Sea Water<br />

and Whirled Sea sand <strong>of</strong> TiN-coated Stainless <strong>Steel</strong>”, Thin Solid Films, Vol. 137, No.<br />

1, pp 59-63.<br />

Metal <strong>Coating</strong> International Inc. 1998, DACROTISING & DACROSEALING. <strong>Coating</strong><br />

serving. Industry Worldwide, Chicago.<br />

Mosser M.F. & McMordie B.G. 1994, “Evaluation <strong>of</strong> Aluminium/Ceramic <strong>Coating</strong>s on<br />

Fasteners to Eliminate Galvanic <strong>Corrosion</strong>”, Technical Paper <strong>of</strong> SAE (Australia), No.<br />

860112, pp 47-58.<br />

Ridder J.A. 1995, “<strong>Coating</strong>s Meet Standardisation Trend”, Fastener Technology<br />

International, No. 5, pp 45-47.<br />

Termosil Asia Sdn Bnd 1997, TERMOSIL. The Ultimate Anti-<strong>Corrosion</strong> <strong>Coating</strong><br />

Technology, Singapore.<br />

White R.W. 1995, “Double Teaming the Elimination <strong>of</strong> Cadmium. (Part 1)”, Fasteners<br />

Technology International, No. 2, pp 78-83.<br />

<strong>Corrosion</strong> <strong>Protection</strong> <strong>of</strong> <strong>High</strong> <strong>Carbon</strong> <strong>Steel</strong> <strong>with</strong> <strong>Duplex</strong> <strong>Coating</strong> System:<br />

Ni-electroless and Termosil<br />

6

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