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Electroplating and Surface Coatings: Chromium Plating, Adhesion, and Friction Behavior - P, Appunti di Ingegneria Meccanica

An in-depth analysis of various surface coating techniques, focusing on chromium plating and its applications. Topics covered include the electroplating process, adhesion mechanisms, and friction behavior of surfaces. The document also discusses the mathematical description of roughness for fractals and the importance of surface cleanliness in measuring coatings' thickness.

Tipologia: Appunti

2019/2020

Caricato il 19/04/2020

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Surface engineering
โ€ข Chromium plating Introduction
Chromium plating is a technique used for metallic substrates (conductive ones in general) which can be:
- Functional, or โ€œhard chromium platingโ€. Its purpose is to produce a relative thick chromium deposit,
which provides one or more specific functions, such as hardness and wear resistance. Typical
thicknesses range from 0.5 to 1000 microns. It is based on solutions containing chromium trioxide
(hexavalent Cr).
- Decorative: thin coatings that are applied most often over a highly-polished surface or over bright
nickel. The purpose is to modify the appearance of the surface to a more pleasing color (faint blue
to black). Thicknesses range from 0.1 up to 1 micron. It can be obtained both from hexavalent and
trivalent chromium, but mostly from the latter. If chromium-3 is used, pollution will be lower and the
process is more flexible (it can be stopped and re-started), but the resulting coating will be weak and
slightly more impure.
Chromium is a metal characterized by a BCC structure that provides high hardness and wear resistance. It
has semi-magnetic property that allows thickness monitoring. It has low heat conductance, low coefficient
of friction and it can reach a hardness up to 1000 Vickers. To deposit chromium over a surface, the process
of electroplating must be introduced: it is an electrochemical process taking place in a tank containing a wet
phase and which allows coating of parts with any size.
โ€ข Electroplating equipment
- Anodes: they can be either soluble or insoluble.
Insoluble ones are made of a lead alloy containing
tin or antimony due to leadโ€™s ability to passivate
(changing colour). Soluble anodes are almost never
used, since they passivate too much (reducing their
conductivity too much) and tend to develop
trivalent chromium. Multiple anodes are used to
allow uniform coating of the component.
- Cathode: it is simply the part that must be plated.
- Heat exchanger: most chromium plating processes require constant temperature. Cooling is
required during operation because of the high current load. Generally, there are two heat
exchangers, one to heat the solution and one to cool it down.
- Tank: it contains the solution. It is generally made of stainless steel coated by polymeric coatings to
protect it from corrosion (all but rubbers). Alternatively, it is possible to use titanium. There is always
a secondary tank that contains the first to avoid leakages if it is damaged. Note that chromium 6+ is
both toxic and carcinogenic, but it gives better properties, not achievable with the trivalent one.
- Electrolytes: the salts of the metal to be deposited are dissolved in the solution. Commercial
electrolytes contain a lot of chemicals to increase conductivity and modify the coating properties
and they are generally aggressive towards the equipment and the environment. In particular, sulfuric
acid must be dissolved in the solution in a 1/100 ratio compared to chromium as it is a catalyst and
coordinates to the chromate ions (nowadays ๐นโˆ’ based substances can be used).
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Scarica Electroplating and Surface Coatings: Chromium Plating, Adhesion, and Friction Behavior - P e piรน Appunti in PDF di Ingegneria Meccanica solo su Docsity!

Surface engineering

โ€ข Chromium plating Introduction

Chromium plating is a technique used for metallic substrates (conductive ones in general) which can be:

  • Functional , or โ€œhard chromium platingโ€. Its purpose is to produce a relative thick chromium deposit,

which provides one or more specific functions, such as hardness and wear resistance. Typical

thicknesses range from 0.5 to 1000 microns. It is based on solutions containing chromium trioxide

( hexavalent Cr).

  • Decorative : thin coatings that are applied most often over a highly- polished surface or over bright

nickel. The purpose is to modify the appearance of the surface to a more pleasing color (faint blue

to black). Thicknesses range from 0.1 up to 1 micron. It can be obtained both from hexavalent and

trivalent chromium, but mostly from the latter. If chromium-3 is used, pollution will be lower and the

process is more flexible (it can be stopped and re-started), but the resulting coating will be weak and

slightly more impure.

Chromium is a metal characterized by a BCC structure that provides high hardness and wear resistance. It

has semi-magnetic property that allows thickness monitoring. It has low heat conductance , low coefficient

of friction and it can reach a hardness up to 1000 Vickers. To deposit chromium over a surface, the process

of electroplating must be introduced: it is an electrochemical process taking place in a tank containing a wet

phase and which allows coating of parts with any size.

โ€ข Electroplating equipment

  • Anodes : they can be either soluble or insoluble.

Insoluble ones are made of a lead alloy containing

tin or antimony due to leadโ€™s ability to passivate

(changing colour). Soluble anodes are almost never

used, since they passivate too much (reducing their

conductivity too much) and tend to develop

trivalent chromium. Multiple anodes are used to

allow uniform coating of the component.

  • Cathode : it is simply the part that must be plated.
  • Heat exchanger : most chromium plating processes require constant temperature. Cooling is

required during operation because of the high current load. Generally, there are two heat

exchangers, one to heat the solution and one to cool it down.

  • Tank : it contains the solution. It is generally made of stainless steel coated by polymeric coatings to

protect it from corrosion (all but rubbers). Alternatively, it is possible to use titanium. There is always

a secondary tank that contains the first to avoid leakages if it is damaged. Note that chromium 6

is

both toxic and carcinogenic, but it gives better properties, not achievable with the trivalent one.

  • Electrolytes : the salts of the metal to be deposited are dissolved in the solution. Commercial

electrolytes contain a lot of chemicals to increase conductivity and modify the coating properties

and they are generally aggressive towards the equipment and the environment. In particular, sulfuric

acid must be dissolved in the solution in a 1/100 ratio compared to chromium as it is a catalyst and

coordinates to the chromate ions (nowadays ๐น

โˆ’

based substances can be used).

  • Stirring system : it is used to speed up the kinetics of the process (reducing the diffusion layer ). Itโ€™s

generally either a bubbler , a mechanical stirrer or a filtration system, the latter being very good at

removing contaminants, which may be deleterious: dust particles may be embedded into the coating,

thus reducing the performances. It is also possible to stir the solution by means of pumps , but these

are usually used only during the deposition of composites. Stirring is also useful to compensate for

the tip effect , the concentration of electromagnetic fields on the tips of the material. This

phenomenon usually causes selective thickening in the coating.

  • Exhaust gas hood : it is used to control the emission of pollutants. Fume suppressants are also

employed. During the process, a high amount of gases are produced (mainly hydrogen and oxygen ).

  • Chemistry of the solution

The solution contains chromic acid in high concentration. It has acidic behavior and it dissociates in the

solution as:

3

2

2

4

2

4

4

2 โˆ’

While at high concentrations as:

2

4

2

2

7

2

2

2

7

2

7

2 โˆ’

The reduction of chromium takes place at the surface of the component being plated. Generally, the process

is catalyzed by the presence of sulfate anions (without it the reduction to metallic chromium is not feasible).

2

7

2 โˆ’

โˆ’

2

There are also side reactions that reduce the efficiency of the process (max efficiency 20% ):

โˆ’

2

2

7

2 โˆ’

โˆ’

โˆ’

3 +

2

On the anode , we observe the evolution of oxygen. This leads to a buildup of oxygen and hydrogen, which

may cause explosions, but oxygen is useful nonetheless: it oxidizes trivalent chromium in the bath to give its

hexavalent counterpart. Note that, as of now, only the hexavalent chromium oxidation state can be used to

produce effective coatings, despite the environmental hazards.

  • Electrolyte bath structure

The electrolyte bath shows a โ€œlayeredโ€ structure, as in the figure below:

1) Electrode (workpiece)

2) Helmholtz double-layer, characterized by a double-layer of localized ions

3) Diffusive layer, where the main phenomenon is diffusion of ions to the electrode

4) Bulk solution (convection of fluids)

see this technique as a combination of the last two, having the highest resolution of all, also giving

maps of surfaces.

  • Interferometry: An electromagnetic radiation is shot towards the sample. Due to the wave-like

properties of light, diffractive and interference phenomena will take place on the surface due to its

rough structure. Resolution is high for this technique and itโ€™s best used for small areas. The output

of the instrument will be a top-down view of the sampleโ€™s surface in false colors, highlighting its

structure (a bi-dimensional map )

  • Laser profilometry : A coherent beam of photons (laser beam) is pointed towards the surface to be

analyzed (contactless analysis). The consequent reflection angle of the beam is measured and the

surface is mapped accordingly. Resolution is very high for this technique, but limitations imposed by

the material itself are common: if the material is too rough or transparent , the surface wonโ€™t be

reflective enough for the beam to bounce off. As in the following technique, the output of the

instrument will be a graph of the surface obtained line by line.

  • Mechanical stylus analysis: A sharp, hard and fine stylus is placed in contact with the surface to be

mapped. The stylus is sensible to roughness bigger than its tip and will move up or down accordingly

when dragged along a straight line over the surface. This movement will trigger an automated

response and the profile of the surface will be mapped, one line at a time. Limitations of this

technique include limited resolution due to the tip radius size and possible degradation (scratching)

of the sample.

  • Parameters for superficial roughness

The parameters used to define a surfaceโ€™s roughness are as varied as the techniques used to measure them.

A brief list and explanation of the most used ones will follow, along with their mathematical expression.

  • Average roughness

The average roughness expresses the mean absolute height of both hills and valleys on the surface,

as expressed in the following:

๐‘Ž

๐ฟ

0

  • Root mean square roughness

Defined in a manner similar to the previous one, but using a geometrical avarage approach:

๐‘Ÿ๐‘š๐‘ 

2

๐ฟ

0

  • Maximum peak-valley height

The highest (or lowest) point is used to define roughness ๐‘…

๐‘ก

, as its name suggests.

  • Average point height

Roughness ๐‘…

๐‘ง

is quantified as the mean heigh of a given set of sample points on the surface.

All these different measures are useful as they depend

on slightly different geometrical features of the surface.

For instance, letโ€™s take into account the two surfaces on

the right, A and B.

For both cases, the average roughness might be equal to 0.25, but due to how itโ€™s calculated, the root mean

square roughness is equal to 0.58 in the first case and 0.37 in the second. Different parameters give different

information on the surface, such as its production process and its life under service.

  • Spatial parameters

Spatial parameters are dependent on the history on the material and consider the effects of superficial

heterogeneity across the entire surface. The most used are the following:

  • ACFV โ€“ auto covariance function

This function expresses the correlation between two shifted points on the surface of the sample, so

as to find a critical length after which the surface repeats itself (๐œ):

(๐œ)

= lim

Lโ†’โˆž

(๐‘ฅ)

(๐‘ฅ+๐œ)

๐ฟ

0

In optical application, the frequency at which a profile is repeated is a must-know.

  • ACF โ€“ auto correlation function

This function is defined as the ACFV โ€œnormalizedโ€ on the root mean square roughness (squared) and

highlights the differences in the roughness before and after wear of the surface.

(๐œ)

๐‘ž

2

Another property dependent on the history of the material (and its superficial wear) is that which defines a

fractal. A fractal is the paragon of self-similarity, a structure which repeats itself perfectly for each scale.

This means that a mathematical description of roughness in dependence to scale is possible for a fractal:

(๐‘ฅ)

(๐ทโˆ’ 1 )

cos

(( 2 โˆ’๐ท)๐‘›)

โˆž

๐‘›=๐‘›

1

Where โ€œGโ€ is the characteristic length scale, โ€œDโ€ is the fractal dimension, which is correlated to the history

(1 for not polished surfaces and 2 for polished ones) and โ€œ๐›พโ€ the density of the spectrum of frequency.

The act of characterizing mathematically a superficial sector of a sample in order to reconstruct another

sector is possible only if the object possesses a property, called self-transformability.

  • Chemical characterization of a surface

The chemical composition of a surface can be examined by means of a variety of techniques:

  • XRD gives information about crystallinity , crystallite size, strains and even composition, derived from the

pattern of the peaks. This technique is both quantitative and qualitative.

  • XPS offers information about the composition of the examined substrate and so also about possible

oxidation. In addition, by means of sputtering, it is also possible to acquire knowledge on the inner layers.

  • SEM/EDX give information about morphology and composition and are superficial techniques.
  • Glow Discharge Optical Emission Spectroscopy gives a profile of composition vs. depth with sputtering

and consequent analysis of the sputtered material.

  • X-Ray Fluorescence spectroscopy gives a measure of the quality of the coating.

The advantages of electro-less plating are the following: more uniform deposition, current-independent

rate, less porous deposits, better abrasion and wear resistance and plating possible on any surface.

The disadvantages are: more expensive (Pd for activation), lower rate , lower thickness , brittle deposits,

higher T (80- 90

o

C), shorter bath life, more chemical control.

The procedure involves cleansing and degreasing of the surface, etching

and then rinsing to remove the used chemicals. After that, the surface is

prepared by sensitization and activation , rinsing is again needed and

then finally electroless deposition itself can take place.

For some metals, such as Ni, Al and steels, activation is not needed. For

other metals, contact with the above, or even application of a cathodic

current, may be needed. For insulators, it is possible to deposit Pd after

immersion in SnCl 2

to increase roughness.

  • Barrel plating

A common technique is represented by barrel plating , where

the parts to be coated are in contact with pieces of steel or

nickel inside a rotating cylinder in order to favor uniform

coating. Note that the oxidation of the reducing agent may also

trigger the deposition of a second element , such as in the case

of Ni-P plating, giving rise to difficult pure metal deposition.

Deposition of stoichiometric alloys is thus more complex than

with electrodeposition, since it is difficult to control the amount

of P and contamination is easier.

Stabilizers are used to prevent dust particle to act as reductive centers toward the metal ions and improve

brightness and uniformity. An excess, however, may cause a reduction of the plating rate.

organic additives are used in solution to form meta- ion complexes , stabilizing the pH and increasing the

deposition rate.

During the process of Ni-P plating, the hypophosphite ion (reducing agent, from sodium hypophosphite) is

catalytically oxidized onto the surface to be plated. This is done to release hydride ions, which are then

available for reduction of nickel ions at the surface. The hypophosphite also undergoes catalytic

decomposition, forming either additional hydrogen or phosphorous. The products of the reactions are thus

the nickel-phosphorous deposit, phosphate ions, hydrogen ions, and hydrogen gas.

Two types of electroless nickel solutions are currently employed; namely acidic (๐‘๐ป = 4 โˆ’ 5. 5 ) and alkaline

solutions (๐‘๐ป = 8 โˆ’ 10 ). The essential constituents of electroless nickel solutions are a soluble nickel salt to

provide nickel ions, and a reducing agent. Other constituents are complexing agents, buffers, solution

stabilizers and rate promoters.

The deposition rate of electroless nickel from acid solutions decreases with decreasing pH. Solutions below

pH 4 are impractically slow. At pH above 5.5, the precipitation rate of nickel is too fast and it leads to bath

instability. On the other hand, the deposition rate of electroless nickel from alkaline solutions is not

significantly affected by pH. These solutions are usually maintained at pH 8 to 10 with ammonium hydroxide

(when ammonium hydroxide runs out the solutionโ€™s color shifts from blue to green).

The phosphorous content of nickel coatings is primarily dependent upon the solution pH; decreasing with

increasing pH. Acid: 2 - 13% , alkaline 3-7%.

A higher phosphorous content of the coating means that:

  • Ferromagnetism and tensile strength decrease;
  • Wear resistance, Salt spray time and corrosion resistance increase.

T emperature is one of the most important factors, affecting the plating rate as an exponential of T.

Turnover : when a mass of nickel equal to the entire nickel content of the tank has been deposited, a

โ€œturnoverโ€ occurred. At this point, the operator may remove the solution from the tank, rinse all

components, passivate/strip surfaces of hardware being used with nitric acid, rinse all hardware, make

chemical modifications to the solution as necessary, and finally return the solution to the tank for further

service. After a certain number of turnovers, the orthophosphate concentration becomes too high (>

300 ๐‘”/๐‘™), and the solution must be either purified or recycled. 10 turnovers are the minimum number for a

well-engineered process.

  • Electroless Plating - heat treatments

Heat treatments tend to alter the structure of the electroless deposit, from an amorphous to a crystalline

nickel structure containing insoluble micro-particulates of ๐‘๐‘–

๐‘ฅ

๐‘ฆ

and ๐‘๐‘–

๐‘ฅ

๐‘ฆ

alloys. The composition of these

compounds will depend on the temperature-time relationship, the cooling rate after heat treatment and

type and amount of internal stresses in the deposit. The most commonly found compound is ๐‘๐‘–

3

Heat treatment of Ni-P and Ni-B electroless alloys will result in an increase in hardness under the right values

of temperature and time, which are typically optimized for each alloy and substrate combination. Higher

temperatures typically produce maximum hardness in a short period. Heat treatment for excessively long

periods can reduce the hardness well below the optimum values.

  • Electroless Plating- nickel phosphorous types
    • High phosphorous (> 10%๐‘ƒ): Offers a combination of excellent corrosion resistance and reasonable

wear resistance. It is not ferromagnetic. It has low hardness values (850 VHN after heat treatment).

  • Mid phosphorous ( 6 โˆ’ 9%๐‘ƒ): Better solderability, faster deposition rate, higher hardness, cheaper,

but lower corrosion resistance.

  • Low phosphorous ( 2 โˆ’ 4%๐‘ƒ): Offers the highest hardness, both before and after heat treatment ( 700

up to 1050 VHN). Best solderability, cheapest, but has the lowest corrosion resistance.

  • Thickness measurements

The main methods which are used to measure thickness are:

  • Dropping tests
  • Microscopic
    • Coulometric stripping
    • Beta backscatter
      • Eddy current
      • X-ray

Dropping test : it is used to determine the coating thickness in areas not accessible to measurements using

probes. Usually employed for Zn, Cd, Sn and Cu. Precision is around 15%. During the test, a corrosive solution

is dripped on the coating until the latter is penetrated.

Coulometric stripping test : the device consists of an instrument housing a small test cell which is placed on

the test sample. The test cell is in contact with the sampleโ€™s surface by means of a small rubber gasket, which

prevents leaks The cell is filled with an electrolyte , through which current passes, dissolving the coating. The

sample serves as the anode. The test stops when there is an abrupt change in the applied current or potential,

indicating that the coating is fully dissolved. Knowing the area and the charge required, thickness is

determined. A direct relationship between time needed and thickness can be obtained. Many factors can

force required to peel the deposit is recorded. Results are influenced by the angle of peel, rate of

peel, thickness, and width of the strip. The peel values are divided the force necessary to initiate

peeling or the force necessary to continue peeling at steady state, and are given as force/length. The

adhesion can be estimated by how far from the detachment line of demarcation the deposit is peeled.

  • Corrosion tests

Most of the following tests are based on accelerated corrosion, developed to give results in a shorter time

than field exposure.

  • Salt spray : the 5% salt spray test is the most widely used corrosion test. The test may be made more

aggressive by changing the pH with acetic acid (common for zinc-based alloys) or copper based acids,

the latter being even more aggressive. The number of days the coating resisted is counted.

  • Corrodkote test : it evaluates the corrosion protection of a decorative copper-nickel-chromium

deposit on either steel or zinc based alloys. A slurry containing cupric nitrate, ammonium chloride and

kaolin Is used to test panel or product. The film is allowed to dry before exposing the part to humidity.

The temperature is fixed at roughly 38ยฐC. and A single period of 20 hours is considered one cycle. The

sample is then removed from the humidity chamber and visually examined for signs of corrosion.

  • Humidity test : used alongside other corrosion tests it can detect retained residual plating solutions

embedded in the film. It can be used to artificially age coatings prior to some tests. Humidity tests are

also used to evaluate the adhesion and performance of paints. Total immersion, partial immersion

and cyclic immersion tests with water or diluted electrolyte solutions are also used alongside high

temperatures.

Other tests include:

  • Porosity tests
  • Hardness tests
  • Porosity tests
  • Residual stresses tests
    • Ductility tests
    • Hydrogen embrittlement tests
    • Surface roughness tests
    • Wear tests
  • Surface forces and adhesion phenomena

The study of superficial forces is paramount to understanding how and why phenomena like adhesion and

friction occur. In this chapter said forces shall be introduced and modelled.

Firstly, one must define what a superficial force may originate from. Three main types exist:

  • Chemical forces (chemical bonds)
  • Mechanical forces (mechanical interlocking)
  • Physical forces (dipoles, chargesโ€ฆ)

In the case of electrostatic forces one can identify three main types of interaction:

  • Keesom โ€™s dipole - dipole attraction,
  • Debie โ€™s dipole - induced dipole attraction,
  • London โ€™s induced dipole-induced dipole attraction, also known as Van der Waals bonds.

These forces have conventionally been studied on extremely small particles, interacting either with a surface

or another particle. From these experiments a common result emerged: adhesion forces are strictly short-

range interactions , able to take hold of the particle only for distances in the order of the nano/micrometer.

One way in which these forcesโ€™ potential is modelled was proposed by Mie , a purely empirical expression:

1

๐‘›

2

๐‘š

From this expression stemmed other, more specific ones, in which the values C, n and m gain a somewhat

physical value. One of such expressions is the Lennard-Jones potential, in which ๐‘› = 6 , ๐‘š = 12.

Note that, the higher โ€œnโ€ gets, the more โ€œshort rangeโ€ the attractive force becomes. Long range interactions,

such as gravity, can be modelled with ๐‘› = 1 , for instance.

This model proved invaluable, but probably managed to give the reader a

false sense of scale. As a matter of fact, this dependence on range is a

consequence of the microscopic nature of the particle under study, making

it unsuitable to model two vast, planar surfaces interacting with each other.

In order to develop a better model, one needs to consider a real particle of

radius โ€œRโ€, computing the above expression for the radius of the particle

tending to infinite. If thatโ€™s the case, its curvature will tend to zero and a

simple, infinite surface will be left. For ๐‘› > 3 we have a potential:

๐‘›โˆ’ 3

Thus, if we put n=6 like in the L.J. case, it is possible to note that the behavior is different, since we are not

referring anymore to single molecules or atoms, we have a bigger scale of interaction:

3

Let us consider for example a coulombic attractive force between a particle and a surface of infinite depth

and width. One such particle shall feel a coulombic potential quantified by the well-known expression:

( ๐‘™

)

1

2

0

๐‘Ÿ

The coulombic attractive force will be given by the first derivative over the distance, which in turn will result

in the following expression, where ๐œŽ will be the charge density on the surface:

( ๐ท

)

0

๐‘Ÿ

[

2

2

โˆ’ 1 ]

The above shows that, for a particle radius tending to infinity (๐‘… โ†’ โˆž) the resulting attractive force shall be

independent from distance , equal to a constant which only depends on the environment:

๐’”

๐ŸŽ

๐’“

This expression means that, in real surfaces , attractive forces are actually a form of long-range interaction.

Clearly, in real cases no infinitely wide surface is possible, thus forces do not actually have an infinite range.

The above expression also highlights the importance of the medium between the two surfaces, especially in

physical, electrostatic interactions. Said medium can either strengthen the attractive force ( adhesive ) or

A different phenomenon is that of elasto-hydrodynamic lubrication , where surfaces are not conformal and

the pressure largely increases due to the confinement of the load to a small area. Here the lubricant may

behave as a solid , since:

0

e

(๐›ผ๐‘ƒ)

This can cause load transfer and deformation of both surfaces.

In boundary lubrication the separation is only of few hundreds of

nanometers, obtained either by physical absorption (VdW forces) or by

chemical absorption (covalent bonding and self-assembled monolayer). This

will modify the chemical and the physical contribution to friction, leaving the mechanical one unchanged.

Steric occupation of the space also opposes the applied load, giving a form of repulsion.

On the boundary between boundary and mixed lubrication, the two surfaces are not completely separated

and between them lies a film of lubricating โ€œboundary additivesโ€. These are so called because they protect

the two surfaces from wear, but they have not been characterized yet.

  • Chromium friction behavior

Cr is used both for low-friction and wear-resistant applications. The amount of material lost to wear can be

quantified as:

Where H is the hardness, W the load and K a proportionality constant. Given the hardness of Cr, its wear

resistance is also high. Chromium layers also tend to be flat , preventing interlocking. In addition, the

microcracks can also retain lubricant , while the overall surface energy is low thanks to the natural passive

oxide on the surface. Chloride may however cause corrosion at the interface by slipping through the cracks,

which can be prevented by: filling them with lubricant, forming Ni-P or Ni interlayers, or by growing different

layers of chromium instead of only one. the latter can be done only by lapping (cleaning) the surface before

starting again, in order not to cause cohesion failure due to oxidation.

  • Zinc Coatings

These coatings are widely diffused as a mean of corrosion prevention, due to zincโ€™s low โ€œnobilityโ€ and its

uniform corrosion behavior. In addition, these surfaces can be easily modified by conversion coating

technologies to further improve corrosion, to affect the friction coefficient and to give a better anchoring for

paints. As for the possible existing deposition methods, we will examine the following:

1. Zinc Electrodeposition (ECD) : the applied material can be cheap, pure zinc, but also alloys such as ZnNi

(Ni 12%). The latter produces a specific crystalline phase ( ๐œธ ) , which increase the corrosion resistance (in

the order of hundreds of hours at the salt spray test). Different electrolytes can be used, either acidic or

alkaline ones, the former having higher efficiency. Economic considerations impose a limit on the use of

cyanide-based reagents. The problems arising from this method are due to side reactions of

electrodeposition, which enhance the risk of hydrogen embrittlement. The deposited thicknesses are of

the order of few ๐œ‡๐‘š.

2. Hot Dip Galvanizing (HDG) : pure molten zinc is used, since ๐‘‡ ๐‘š

๐‘๐‘›

๐‘œ

๐ถ. The interface between layer

and substrate will not be as sharp as in the previous case ( diffusion ). As a matter of fact, the presence of

intermetallic compounds is inevitable since in the molten zinc will dissolve in the iron and vice versa,

giving precipitation of compounds with a gradient percentage of the two elements. This affects both the

mechanical properties and the corrosion resistance.

Usually the top layer will be pure zinc, which offers the best resistance to corrosion. Depending on the

percentage of the two elements, a hard ๐œน phase might be present, which offers high wear resistance.

Thus, the process should be tuned to achieve a desired thickness of the ๐›ฟ layer. The deposited thicknesses

are of the order of some hundreds of ๐œ‡๐‘š, which may cause weight issues. Also, some steels will diffuse

so fast into the zinc layer to cause various problems.

3. Zinc Flakes : used for bolt fabrication, this technique is also referred to as Zn paint , since it is a mixture of

Zn and Al particles (100 ๐œ‡๐‘š) and epoxy resin, with silane sizers. The coating can be applied either by

spraying, dipping or in a centrifuge and the structure is composed of lamellae of zinc held together by the

resin, which provides a physical barrier and lowers the friction coefficient. The finish will be matte and

not bright, but the thickness is very uniform (< 10 ๐œ‡๐‘š, tipically 4+4) and the coating can be easily colored.

4. Mechanical Zinc : A reactor contains a solution of Zn particles (typically a suspension, with surfactants to

avoid conglomeration) and hard spheres. A rotation is imposed to the system and the spheres will spread

Zn on the top of the component, with metallic bonding or interlocking. Thus, the deposited material will

be pure Zn, with thickness of the order of 10 ๐œ‡m.

5. Sherardization : this is a solid-state diffusion process used for large components. The process consists of

putting in contact the component with zinc at high enough Tโ€™s (enough for inter-diffusion, but not melting)

and the result is a layered structure of intermetallic compounds. The thickness will be dependent on the

time of the process and is generally around 100 ๐œ‡m.

  • Chromate conversion coating

Chromate conversion coatings are chemically generated layers, on zinc and other metals. The combination

of zinc , to sacrificially protect the steel, and the chromate film, to enhance the appearance and improve the

corrosion resistance of the zinc, makes it one of the most appealing solutions in coating industry.

The appearance of the coating is able to match the electroplated chromium, reaching similar levels of polish

and specular reflectivity. The brightness and uniformity of color on the finished product are then greatly

enhanced. Moreover, chromate films also enhance paint adhesion to zinc coated/plated parts.

The amorphous trivalent chromium oxide provides a mechanical barrier against abrasion. Although

chromate coatings have relatively low abrasion resistance, they are still good enough for mild-wear

applications. Cold forming operations are usually possible. Films can also be soldered, but it must be

remembered that they are damaged by heat. As a result, a large area of chromate film around the solder

joint is damaged by the soldering temperature.

The color of the film is determined mainly by the amount of entrapped hexavalent chromium, by the

insoluble trivalent chromium and the catalyst that complex them. The color allows the definition of four

major types of conversion coatings for zinc:

  • Clear or Blue-bright : it is primarily used to provide a decorative finish.
  • Yellow : it provides a good corrosion protection. It is used in the automotive field, computer hardware,

appliance, and other industries where good corrosion resistance is necessary.

  • Olive drab: it offers the maximum corrosion protection over zinc and it requires hexavalent chromium

based systems.

  • Black : it offers a very good corrosion protection. The most expensive formulations can reach a values

equal to that of olive drab coatings.

Chromate conversion coatings are easily dyed , which can be for color-coding of parts.

  • Conversion Process

Phosphate coatings are produced by converting some of the soluble phosphate to insoluble phosphate

compounds. To crystallize any inorganic compound, the solubility of that substance must be exceeded,

usually by cooling down an oversaturated solution, or by changhin pH and chemical content near the surface

of our part. pH increases due to the dissolution of the substrate metal, which releases hydrogen gas,

depriving the solution of ๐ป

ions. The dissolved metal increases the salt content above the solubility level,

initiating the crystallization process. Depending on the chemical constituents and conditions of temperature

and agitation, more than one phosphate compound can crystallize out of the solution.

The largest application for phosphate coatings is as an intermediate for bonding paints. Such coatings

substantially improve adhesion, impact resistance and flexibility of paint films and prevent the rusting of the

underlying metallic part in case of failure of the paint.

There exist different types of phosphate coatings:

  • iron phosphate coatings: excellent adhesion and good corrosion resistance;
  • zinc phosphate coatings: excellent corrosion resistance and superior paint bonding;
  • manganese phosphate coatings: good corrosion resistance, porous structure holds oil reservoir.

These compound coatings are made of very small interlocked crystals which create a very intricate structure.

This structure is porous and allows a very good mechanical adhesion , acting as an oil reservoir.

Zinc phosphate : commonly used as an under-coat for paint, it improves adhesion and corrosion resistance

of the part, even if the paint is slightly damaged. Corrosion resistance is high, even though synthetic oils can

prove detrimental. The crystals also act as lubricants in cold metal deformation applications. Zinc phosphate

has several advantages over iron phosphate. The crystal size can be controlled by the addition of modifiers

or surface conditioners prior to the process. Zinc phosphate also provides an excellent oil storage and the

corrosion resistance is dependent upon the quality of the applied oil. Under paints, zinc phosphate offers

better adhesion, corrosion resistance and impact resistance. Visual examination is employed to check the

quality of the coating. Zinc phosphating processes are organized as follows:

  1. alkaline cleaning
  2. water rinsing
  3. surface conditioning
    1. zinc phosphating
    2. water rinsing
    3. acid rinsi

Iron phosphate: an iron phosphating solution generally consists of alkali metals or ammonium dihydrogen

phosphate. Oxidizing agents , such as nitrites or chlorates, often are used to aid in the phosphating process

by increasing the rate of coating formation. Efficiency is always less than 10%, because competing

intermediate reactions take place. The principal competing reaction is the oxidation of the (primary) ferrous

phosphate to form the very insoluble ferric phosphate, which precipitates from the solution as sludge.

Manganese phosphate : Highest corrosion resistance of all the phosphates. In addition, these coatings are

excellent in abrasive wear applications. It is generally performed on components where electrolytic solutions

may become trapped, causing localized corrosion phenomena, or where no good rinsing with acidic chromic

acid solution can be performed. Different process phases are:

  1. Cleaning of the surface
  2. Rinse
  3. Pre-condition
  4. Phosphating: 10/15min at 95ยฐC
    1. Rinse
    2. Dry
    3. Lubricate with solid lubricants(optional)

Phosphating and electro-painting procedure: electrochemical technique for applying paint to a metal

surface. The part to be painted is made either into an anode or a cathode. the paint, under the influence of

an electric field, migrates to the surface of the metal and becomes insoluble due to an electrical

neutralization phenomenon. The deposited paint acts as an insulating film causing deposition to occur

uniformly over all surface areas of the part.

A properly cleaned surface is critical for the phosphate layer. Traces of soil , areas of light oxidation or

polymerized oi l will affect the phosphate conversion coating appearance. Any irregularities will be magnified

during the painting process. At the end of the process it is necessary to perform a chromic acid rinsing , which

enhances corrosion resistance and minimizes rusting during line stoppage. The benefits of this final rinse are:

  • Improved corrosion resistance : the solution efficiently seals the pores of the coating.

  • Improve paint adhesion : The sealing ability of chromate stops the pores from reducing film adhesion

  • Minimizes filiform corrosion
  • Reduces paint blistering
  • Minimizes rusting of parts during line stoppage
  • Degradation phenomena

Surface degradation can have different causes:

  • Adhesion : two surfaces in relative motion with each other may have a partial electronic cloud

superposition. If high, degradation will be quicker. To minimize this, we must choose a proper

combination with low chemical compatibility.

  • Abrasive wear : it is a phenomenon caused by the presence of abrasive particles between two surfaces

in relative motion. these can be present due to:

  • Ploughing
  • Brittle fracture
    • Grain detachment
    • External environment

If the particle hardness is just slightly higher than that of the surface, wear rate increases dramatically. To

reduce it, itโ€™s necessary to reduce the grain size or increase the hardness. Abrasive wear can also be

exploited, such as in polishing.

Erosion : wear process caused by the impact of particles (solid or liquid) against a surface. It can be

macroscopic, at the atomic scale or due to cavitation. The main parameters to consider are:

  • Phase of the particles
  • Shape/size
    • Angle of impingement
    • Velocity

Small and slow particles with low angle of impingement cause a sort of abrasion, while high-angle ones can

induce plastic deformation of the surface. Big and fast particles can induce local melting of the surface,

changing the local mechanical properties. Erosion can occur also at the atomic scale, due to local

displacement of atoms and an increase of surface energy. When surface energy becomes too high, cracks

nucleate on the surface, to obtain a lower energy configuration. In cavitation : bubbles collapse at the

interface between a liquid and the material. If the released force is high enough, detachment of particles

from the surface may occur.

Other wear-inducing phenomena include:

  • Fretting : similar to abrasive wear, but the removed material is not ejected from the contact area. It

is much more aggressive than abrasive wear and it requires a special design of the contacts. Hard

chromium is extremely bad for preventing this phenomenon, as it releases hard particles.

  • Melting wear : the heat generated during surface sliding may induce local melting of the surfaces.

Usually melting concerns asperities since they have a lower melting point compared to the bulk

material. If oxygen is present, oxidation may occur with modification of the surface properties.

  • Diffusion wear : high stresses and temperature may cause diffusion of material from one surface to

the other. This causes a modification of surface properties.

  • Fracture, fatigue, creep : all of these may cause failure of the component.
  • Chemical action : the main chemical degradative phenomena are related to reactions in water, high

temperature oxidation and biochemical processes.

  • DVD

DVDโ€™s have the same size of standard CDโ€™s, but theyโ€™re made by two substrates glued together. The possibility

to use two layers for data storage allows to have 4 different formats (5, 10, 9, 18) with different capacities.

In DVDโ€™s, tracks have a lower distance and lower pitch dimensions. This allows for higher data capacity , but a

lower wavelength laser is also needed to read the data. Blu-ray discs take this to the extreme, with smaller

track distance and even lower pitch dimensions. They require a blue laser to read the data (405nm).

  • Anodization processes

In this process, the component to coat plays the part of the anode , in order to get an

oxide coating. In addition to Al , also Zr and Mg can be anodized, due to their oxides

being stable and hard.

Acidic electrolytes are generally preferred over basic ones and thickness and porosity

can be fine-tuned depending on the type used. Basic electrolytes give non-porous ,

thin coatings.

Aluminum is particularly good for this process, as the resulting oxide layer wil be homogeneous, conformal

and with no โ€œedge effectโ€, unlike in plating. This issue is only present at the beginning of the process, because

of the distribution of current lines, but it will self-regulate with growing thickness, as the oxide is not

conductive. The final thickness will depend on the voltge and on the type of material.

Anodizing leads to an increase in volume , which must be controlled, but there are no adhesion issue during

the problem. Anodizing alloys is possible, but complex, as compounds may form on the surface and alter the

electrochemical activity. These compounds will not dissolve in the bath and are usually inert , which will lead

to the creation of big pores on the surface. This problem must be solved through careful etching.

Another feature of the process is the co-precipitation of sulphate salts (low

percentages) and the entrapping of water and alloying elements, coming

from precipitates or contaminants. The final structure spots porous

hexagonal cells , with a compact barrier layer at the interface with the

component. A post-treatment to close these pores (sealing) is mandatory.

The general temperature of the process must be controlled, as lower T โ€™s (up

to 0

o

C) imply better properties. Since the coating is essentially inert and non-

conductive, the potential step must be smooth, to prevent burning.

Due to Faradayโ€™s law, the thickness of the oxide layer should theoretically

increase with time, but in reality it reaches a plateau: growth is faster at the

beginning, but then it decreases. By examining the Al case, we know that itโ€™s

unstable in both alkaline and acidic media: the growing rate will thus be a

balance between the chemical etching and the actual deposition.

Hard anodizing is a technique based on sulfuric acid, witch employs additives, low temperatures, high current

densities and vigorous agitation. It provides good hardness (300-450 DHN), abrasion resistance, a large

breakthrough voltage, low porosity and high heat resistance.

Soft anodizing can be obtained if the only interest is corrosion resistance. It is performed with high Tโ€™s, higher

solution concentration and lower voltages.

Brightness is usually controlled through roughness and by means of etch-dipping. there are three ways:

  • Nickel-acetate seals : the solution will be absorbed in the porous structure. A thermal treatment then

causes evaporation of the solution and deposition of the salt, an insoluble, mixed hydroxide acetate

of Ni and Al.

  • Water sealing : As above, but the deposited material is Al hydroxide.
  • Use of PTFE.

Lastly, in order to color the component, pigments can be introduced in a suspension just before sealing, or

directly during anodization (electro-coloring). The latter can be problematic since, pigments can stop the

growth of the layer like precipitates. Over time, pigments can react with the environment, giving

discoloration, against which electro-coloring is more resistant.

To reduce both porosity and internal stresses, pulsed anodizing can be used. This technique gives higher

growing rates, but requires more expensive power suppliers.

  • CVD

Vapor deposition gives higher hardness and wear resistance. Its advantages over other techniques are:

  • More controlled environment with lower risk of contamination;

  • Possibility to use plasma both to prepare and to deposit on the surface, the former also in combination

with wet processes;

  • Capability to follow the geometry precisely and to provide a very conformal coating.

As drawbacks:

  • The dimension of the component is directly related to that of the chamber, an issue for large parts;
  • Its deposition rate is lower than that of PVD;
  • The typical achievable thickness is only of few microns;
  • Higher temperatures are needed (up to 1100

o

C), which limits the material of the component.

Gaseous precursors, such as Ti and Al chlorides, must be

combined with other species (and inert gas) to give

adequate reactions. The flow of gas must be optimized to

have a sufficient flow at the surface. Thanks to the high

temperatures, the reaction takes place on the surface

only: rearrangement to form a perfect lattice is highly

favored. An important parameter to control is ฮ”๐บ

๐‘‰

, since

too negative values impede rearrangement (too high

nucleation rate).

Nowadays, even metalorganics species are being

employed to increase the number of feasible precursors, but this process is still rather expensive.

Pure nickel can be deposited on any substrate via CVD (not only conductive), which is impossible by means

of any other technique (electroless deposits compounds). A special case of CVD is that of oxidation reactions ,

such as in the case of quartz coatings , where silica is used, along with self-assembled monolayers of silanes

for anti-fingerprinting applications. CVD is also employed for carbon-nitrides , which combine insulating

properties with hard coating. By choosing the accurate precursor, it is also possible to obtain various coating

structures, such as multilayer, gradient and super-lattices coatings.