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    Unit - II

    UNIT II CORROSION AND CORROSION CONTROL

    Chemical corrosion Pilling Bedworth rule electrochemical corrosion

    different types galvanic corrosion differential aeration corrosion factors

    influencing corrosion corrosion control sacrificial anode and impressed

    cathodic current methods corrosion inhibitors protective coatings paints

    constituents and functions metallic coatings electroplating (Au) and electroless

    (Ni) plating.

    Lecture Session No: 10 Topic: Chemical corrosion, corrosion due to Oxygen

    Pilling Bedworth rule on corrosion products

    Introduction:

    Metals exist in nature in combined state as their oxides, carbonates, chlorides,

    sulphides etc. They are reduced to their metallic state during extraction. When metals

    are exposed to environment their surfaces begin to decay as they come in contact with

    gaseous or liquid environment. This process of deterioration and ultimate destruction

    of a metal due to its reaction with the surrounding is called Corrosion. During

    corrosion the metals exhibit their natural tendency to revert to their native combined

    state of existence as oxides, sulphates, carbonates etc. The most familiar example for

    corrosion is Rusting of iron when exposed to atmospheric conditions. During this a

    layer of reddish scale and powder of oxide (Fe2O3) is formed. All metals and alloys

    are susceptible to corrosion under different environmental conditions. Only metals

    such as gold and platinum exist in nature as metals and are not susceptible to

    corrosion under ordinary atmospheric conditions and hence are called noble metals.

    Corrosion causes a heavy loss to industries since the modern day domestic and

    industrial applications uses mainly metals and alloys.

    Types of Corrosion:

    Corrosion may be broadly classified into two types based on the mechanism of

    corrosion. These include

    (a) Dry corrosion (or) chemical corrosion

    (b) Wet corrosion (or) electrochemical corrosion

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    (a) Dry Corrosion:

    One of the most common ways by which metals get corroded is by direct

    interaction with atmospheric gases such as oxygen, hydrogen sulphide, halogens,

    sulphur dioxide, oxides of nitrogen. Oxygen is primarily responsible for corrosion of

    most metallic structure as compared to other gases and chemicals.

    Oxidation corrosion:

    Direct attack on metal by oxygen even at ambient temperatures in the absence

    of moisture leads to oxidation corrosion, that is, the formation of the corresponding

    metal oxide, which is normally thermodynamically spontaneous process.

    The oxidative corrosion may be considered to involve the reactions of

    oxidation of the divalent metal to form the metal ion with the simultaneous release of

    electrons and the combination of the electrons with oxygen to form oxide ions.

    M M2+ + 2e-

    O2 + 2e- O2-

    The overall reaction:

    M + O2 M2+ O2- (metal-oxide film)

    Oxidation occurs first at the surface of the metal and the resulting metal oxide

    layer acts as the barrier for further reaction. For oxidation to continue either the metal

    must diffuse outwards or the oxygen must diffuse inwards. In general, outward

    diffusion of metal ions and electrons is likely to be more rapid than inward diffusion,

    due to the fact that cations are smaller in size compared to the oxide ions.

    M Mn+ + ne- (oxidation)

    Mn+

    Mn+ O2-

    Mn+

    e- O2-

    Metal-M O2-

    O2 + 2e- O2-(reduction)

    Mechanism of Oxidation of Metal to Metal oxide

    The nature of the oxide formed plays an important role in oxidation corrosion process

    i.e. Metal + oxygen metal oxide (corrosion product)

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    Atmospheric

    oxygen

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    When oxidation starts, a thin layer of oxide is formed on the metal surface and

    the nature this film decides the further action. If the film is:

    (i) Stable: A stable layer is fine-grained in structure and can get adhered tightly to the

    parent metal surface. Such a film behaves as protective coating in nature, thereby

    shielding the metal surface. The oxide films on Al, Sn, Pb, Pt, cu etc., are stable.

    (ii) Unstable: the oxide layer formed decomposes back into the metal and oxygen

    Metal oxide Metal + Oxygen

    Consequently, oxidation corrosion is not possible, thus metals like Ag, Pt, Au do not

    undergo oxidation corrosion.

    Unstable metal oxideExposed area

    Metal +O2 Metal metal oxide Metal + O2 decomposes

    (iii) Volatile: the oxide layer volatilizes as soon as it is formed, thereby leaving the

    underlying metal surface exposed for further attack. E.g. Molybdenum oxide MoO3

    Exposed area Volatile metal oxide

    Fresh surface

    Metal +O2 Metal metal oxide Metal exposed forFurther attack

    volatilizes

    (iv) Porous: having pores or cracks on the surface of the metal, atmospheric corrosion

    have access to the underlying surface of metal, through the pores or cracks of the

    layer thereby the corrosion process continues till entire metal is completely converted

    into its oxide.

    Exposed area porous metal oxide

    Metal +O2 Metal Further attack throughpores/cracks

    continues

    Pilling and Bedworth rule:

    According to Pilling and Bedworth, the oxidation resistance of a metal is

    related to the specific or molar volume ratio of the corrosion product, namely, the

    metal oxide and the metal. It is expressed mathematically as,

    R = (M/D) x (d/m)

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    Where M and m are the molecular weight and atomic weight of the metal

    oxide and the metal respectively, D and d are the densities of the oxide and the metal

    respectively. The ratio r indicates the volume of oxide formed from a unit volume of

    metal. If R1, as in the case of copper-oxygen

    system the oxide is able cover the metal surface effectively. The strongly adherent

    non-porous oxide layer protects the metal from further oxidation.

    Dry corrosion by other gases and chemicals:

    Other gases present in the working environment such as chlorine, fluorine,

    sulphur dioxide, hydrogen sulphide and oxides of nitrogen are also corrosive.

    Hydrogen embrittlement:

    Hydrogen sulphide attacks metals forming the corresponding metal sulphide

    and releases atomic hydrogen. The atomic hydrogen diffuses readily into the metal

    and collects at the void spaces where it combines with atomic hydrogen to from

    hydrogen gas. The accumulation of the gas develops a high pressure causing cracks

    and blisters in the metal. The condition is known as hydrogen embrittlement.

    Decarburization:

    The atomic hydrogen on coming into contact with steel combines with the

    carbon of steel to form methane gas which collects in voids. As the pressure

    increases due to the accumulation of the gas cracks occur in steel, a condition known

    as decarburization.

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    Unit - II

    Lecture Session No: 11 Topic:Electrochemical corrosion Hydrogen evolution

    and oxygen absorption cathodic process, different types galvanic corrosion

    Wet corrosion or electrochemical corrosion:

    The corrosion of metal in aqueous environments is more prevalent than under

    dry conditions. Iron undergoes corrosion to form rust. The rust formed on the

    surface of iron is loose and does not adhere to the metal surface. According to the

    electrochemical theory of corrosion, wet corrosion is a two step process which occur

    simultaneously, namely, oxidation and reduction. The surface of a piece of iron in

    contact with an aqueous solution of electrolyte becomes a galvanic or a voltaic cell

    consisting of anodic and cathodic regions. The galvanic cell formed facilitates the

    flow of positive current from the anodic region to the cathodic region through the

    electrolyte leading to the dissolution or corrosion of the anodic region.

    M M2+ + 2e-

    The electrons are utilized at the cathodic region either to form hydrogen or hydroxide

    ion depending on the pH of the medium. In acidic medium hydrogen is evolved.

    (a) Evolution of Hydrogen:

    This type of corrosion occurs in acidic environment. Considering metal like

    Fe, the anodic reaction is dissolution of iron as ferrous ions with the liberation of

    electrons.

    Fe Fe2+ + 2e-

    These electrons flow through the metal, from anode to cathode, where H+ ions

    are

    eliminated as hydrogen gas.

    Electrolyte

    Iron H+Cl-

    Fe2+ H+Cl-

    2e- H+Cl-

    H2 H+Cl-

    H+Cl-

    Mechanism of Hydrogen evolution

    2H+ + 2e- H2

    The net reaction is Fe + 2H+ Fe2+ + H2

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    This type of corrosion causes displacement of hydrogen ions from the acidic

    solution by metal ions. Consequently, all metals above hydrogen in the

    electrochemical series have a tendency to get dissolved in acidic solution with

    simultaneous evolution of hydrogen.

    In neutral or a weakly alkaline medium, hydroxide ions are formed by the

    reduction of absorbed oxygen

    (b) Absorption of oxygen:

    Rusting of iron in neutral aqueous solution of electrolytes in the presence of

    atmospheric oxygen is a common example of this type of corrosion. The surface

    of iron is, usually, coated with at thin film of iron oxide. However, if this iron

    oxide film develops some cracks, anodic areas are created on the surface; while

    the well-metal parts act as cathodes. It follows that the anodic areas are small

    surface parts; while nearly the rest of the surface of the metal forms large

    cathodes.

    At anodic areas of the metal dissolves as ferrous ions with liberation of

    electrons.

    Fe Fe2+ + 2e-

    Iron Aq. Soln.

    H2O

    Fe2+ H2O

    2e- OH- O2

    H2O O2

    Mechanism of oxygen absorption

    The liberated electrons flow from anodic to cathodic areas, through iron metal,

    where electrons are intercepted by the dissolved oxygen as:

    O2 + H2O + 2e- 2OH-

    The Fe2+ ions and OH- ions diffuse and when they meet, ferrous hydroxide is

    precipitated.

    Fe2+ + 2OH- Fe (OH)2

    If enough oxygen is present, ferrous hydroxide is easily oxidized to ferric hydroxide.

    4Fe(OH)2 + O2 + 2H2O 4Fe(OH)3

    This product is called the yellow rust, actually corresponds to Fe2O3.H2O.

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    If the supply of oxygen is limited, the corrosion product may be even black anhydrous

    magnetite, Fe3O4.

    Types of Corrosion:

    (i) Galvanic Corrosion:

    When two dissimilar metals are electrically connected in the presence of an

    electrolyte, the metal higher up in the electrochemical series becomes anodic and

    suffers corrosion because of its higher oxidation potential. For example if iron and

    copper are connected, here Fe acts as anode i.e. more active metal when compared

    to copper which acts as cathode. Thus the corrosion occurs at the anode and the

    cathode is protected.

    Fe Cu

    More active Less active

    Galvanic corrosion

    The galvanic corrosion may be avoided by a proper selection of metals and

    alloys based on their position in galvanic series.

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    Unit - II

    Lecture Session No: 12 Topic: Differential aeration corrosion factors

    influencing corrosion

    (ii)Differential aeration corrosion:

    This type of corrosion occurs, when one part of metal is exposed to a different

    air concentration from the other part. The parts of the metal exposed to a higher

    concentration of oxygen become cathodic while parts of the metal exposed to a

    relatively lower concentration of oxygen become anodic and get corroded. Example:

    If a metal like Zn is partially immersed in a dilute solution of a NaCl solution is not

    agitated properly, then, the parts above are more strongly aerated and hence, become

    cathodic. On the other hand, parts immersed to greater depth show a smaller oxygen

    concentration and thus, become anodic. So a difference of potential is created, which

    causes a flow of current between the two differentially-aerated areas of the same

    metal. Zinc will dissolve at the anodic areas, and oxygen will take up electrons at the

    cathodic areas to form hydroxyl ions.

    Zn Zn2+ + 2e-

    O2 + H2O + 2e- 2OH-

    Zn rod

    Cathode

    O2 + H2O + 2e- 2OH-

    Anode

    NaCl solution

    Differential aeration corrosion caused by partially immersion of Zn rod

    (iii) Pitting Corrosion:

    Pitting corrosion is a localized accelerated attack. It is usually the result of

    breakdown or cracking of the protective film on a metal at specific points.

    Breakdown of the protective film may be caused by : (i) surface roughness or non-

    uniform finish (ii) scratches or cut edges (iii) local straining of metal, due to non-

    uniform stresses.

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    More oxygenated Cathodic part

    O2 + H2O + 2e- 2OH-

    Iron Pit (Anodic)

    Fe Fe2+ + 2e-

    Pitting corrosion on the surface of Iron

    The presence of the extraneous impurities like sand, dust, scale etc., embedded

    on the surfaces of metals also lead to pitting. Owing to the differential amount of

    oxygen in contact with the metal, the small part underneath the dust or sand becomes

    the anodic areas and the surrounding large parts become the cathodic area. Intense

    corrosion therefore starts underneath the impurity. Once a small pit is formed, the

    rate of corrosion will be increased.

    (iv)Crevice corrosion:

    Crevice corrosion is formed between different metallic objects or between a

    metal and non-metallic material joined by blot, nuts, rivets and washers. The crevice

    on coming into contact with a liquid becomes anodic region as the oxygen supply to

    this area is less compared to other parts and gets corroded preferentially.

    = = = = Anode

    Crevice Corrosion

    Factors influencing the corrosion:

    The rate and extent of corrosion mainly depends on

    1. Nature of the metal

    2. Nature of the environment.

    1. Nature of the metal

    (i) Purity of metal:

    Impurities present in the metal generally form minute or tiny electrochemical

    cells and the anodic parts get corroded. For example Zinc metal containing impurity

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    such as Pb or Fe undergoes corrosion of Zn due to the formation of electrochemical

    cells. Consequently, corrosion resistance of a metal may be improved by increasing

    its purity.

    (ii) Oxidation potential of the metal:

    The position in the electrochemical series is indicative of the natural tendency

    of the metal to undergo corrosion. When two metals are in contact with each other

    and simultaneously with an electrolyte, a galvanic cell is set up and the metal higher

    in the series undergoes corrosion.

    (iii) Overvoltage:

    When a metal, which occupies a high positon in galvanic series for example

    Zn is placed in 1N H2SO4, it undergoes corrosion forming a film and evolvinghydrogen gas, the initial rate of reaction is quite slow, because of high overvoltage of

    zinc metal, which reduces the effective electrode potential to a small value. However,

    if a few drops of copper sulphate are added, the corrosion rate of zinc is accelerated,

    because some copper gets deposited on the zinc metal, forming minute cathodes,

    where the hydrogen overvoltage is only 0.33 V. Thus reduction in overvoltage of the

    corroding metal accelerates the corrosion rate.

    (iv)Passivity of the metal:

    Iron dissolves readily in very dilute nitric acid. However at higher

    concentration acid directly oxidizes the metal to its oxide on the surface. The layer of

    the oxide formed on the surface makes iron resistant to dissolution, a phenomenon

    known as passivity. Passive iron is not easily corroded as the oxide film is self-

    healing, that is, a ruptured film repairs itself on re-exposure to oxidizing conditions.

    (v)Physical state of metal:

    The rate of corrosion is influenced by physical state of the metal such as grain

    size, orientation of crystals, stress etc. The smaller the grain-size of the metal or

    alloy, greater will be the corrosion. Also, the area under stress, tend to act as anodic

    and corrosion takes place at these areas.

    (vi) Relative areas of cathodic and anodic regions:

    The rate of corrosion is more with the combination of a large cathodic region

    and a small anodic region, because the greater demand for electrons at the larger

    cathodic region has to get a greater current density which is supplied by the smaller

    anodic region.

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    2. Nature of the corroding environment

    (i) Temperature:

    With increase of temperature of environment, corrosion rate is generallyenhanced.

    (ii)Humidity in the atmosphere:

    Humidity of the air surrounding the metal influences corrosion, the greater the

    humidity higher being the rate of corrosion. Critical humidity is the humidity of the

    air above which the rate of atmospheric corrosion of the metal increases sharply and

    depends on the nature of the metal and the nature of the corrosion products.

    (iii)Presence of impurities in atmosphere:

    In presence of gases like CO2, H2S, SO2 the acidity of he liquid, adjacent to the

    metal surfaces, increases and its electrical conductivity also increases, resulting in

    higher rate of corrosion.

    (iv) Presence of suspended particles in atmosphere:

    If the suspended particles are chemically active in nature (NaCl) they absorb

    moisture and act as strong electrolytes, thereby causing enhanced corrosion.

    (v) Effect of pH:

    The pH of the surrounding medium plays an important role in influencing the

    rate of corrosion. In general acidic media are more corrosive compared to neutral or

    mildly alkaline media.

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    Unit - II

    Lecture Session No: 13 Topic: Corrosion control sacrificial anode and

    impressed cathodic current methods

    Corrosion Control

    1. Proper designing:

    (i) Avoid the contact of dissimilar metals in the presence of a corroding solution.

    (ii)When two dissimilar metals are to be in contact, the anodic material should have as

    large area as possible.

    (iii) Whenever the direct joining of dissimilar metals is unavoidable an insulating

    fitting may be applied in between them to avoid direct metal-metal electrical contact.

    (iv) A proper design should avoid the presence of crevices between adjacent parts of

    the structure.

    (v) It is desirable that the design allows for adequate cleaning and flushing of the

    critical parts of the equipment. Sharp corners and recesses should be avoided as they

    favor the formation of stagnant areas and accumulation of solids.

    2. Using pure metal:

    Impurities in a metal cause heterogeneity, which decreases corrosion-

    resistance of the metal. Thus, the corrosion resistance of a given metal may be

    improved by increasing its purity.

    3. Using metal alloys:

    Corrosion resistance of most metals is best increased by alloying them with

    suitable elements, but for maximum corrosion resistance, alloy should be completely

    homogeneous. Chromium is the best suitable alloying metal for iron or steel.

    4. Cathodic protection:

    In this method the metal to be protected is forced to behave like a cathode,

    thereby corrosion does not occur. There are two types of cathodic protections:(i) Sacrificial anodic protection method

    (ii) Impressed current cathodic protection

    (i) Sacrificial anodic protection method:

    The metallic structure to be protected is connected by a wire to a more anodic

    metal, so that all the corrosion is concentrated at this more active metal. The more

    active metal itself gets corroded slowly, while the parent structure is protected. The

    more active metal so-employed is called sacrificial anode. The corroded sacrificial

    anode block is replaced by a fresh one, when consumed completely. Metals

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    commonly employed as sacrificial anodes are magnesium, zinc, aluminium and their

    alloys. Important applications of sacrificial anodic method include protection of

    buried pipelines, underground cables, marine structures, ship-hulls, water tanks etc.

    e-

    >

    Mg

    Iron pipe

    Sacrificial anode

    Sacrificial anode cathodic proctection

    (ii) Impressed current cathodic protection:

    In this method the object to be protected is made the cathode of an electrolytic

    cell by connecting it to the negative terminal of a DC source. The positive terminal of

    the DC source is connected to scrap iron, platinum, graphite, nickel or lead anode and

    buried or immersed in a conducting medium adjacent to the metal to be protected.

    The anode is usually in a backfill so as to increase the electrical contact with the

    surrounding soil. This type of cathodic protection has been applied to open water-box

    coolers, water tanks, buried oil or water pipes, condensers.

    e-

    Iron pipe

    Impressed current-cathodic protection

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    Unit - II

    Lecture Session No: 14 Topic: Corrosion inhibitors Anodic, cathodic and VPI

    Inhibitors are inorganic or organic chemical substances which when added in small

    quantity to the aqueous corrosive environment, effectively decrease the corrosion rate.

    Inhibitors are classified as

    (i) Anodic inhibitors

    (ii) Cathodic inhibitors

    (iii) Vapour phase inhibitors

    (i) Anodic inhibitors:

    Oxidizing agents such as sodium chromate and sodium nitrite function as

    inhibitors of corrosion by repairing the protective oxide film or by oxidation of

    corrosion products to less soluble chemicals, which plug anodic sites. These are

    known as anodic inhibitors because they inhibit anodic oxidation of the base metal.

    Anodic inhibitors such as chromates, phosphates, tungstates or other ions of transition

    elements with high oxygen content retard the corrosion of metals by forming a

    sparingly soluble compound with newly produced metal cations at the anodic sites.

    This compound will then adsorb on the corroding metal surface forming a passive

    film or barrier thereby reducing the corrosion rate.

    (ii) Cathodic inhibitors:

    (a) In acidic solutions, the main cathodic reaction is evolution of hydrogen.

    2H+ + 2e- H2(g)

    Consequently, corrosion may be reduced either by slowing down the diffusion

    of hydrated H+ ions to the cathode. The diffusion of H+ ions is considerably decreased

    by organic inhibitors like amines, mercaptans, heterocylic nitrogen compounds,

    substituted ureas and thioureas, which are capable of being adsorbed at the metal

    surfaces.

    (b) In neutral solutions, the cathodic reaction is

    O2 + H2O + 2e- 2OH-

    The corrosion can be controlled either by eliminating oxygen from the

    corroding medium by adding reducing agents like Na2S or Na2SO3 or by retarding its

    diffusion to the cathodic areas by adding Mg, Zn or Ni salts.

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    Unit - II

    Lecture Session No: 16 Topic:Protective coatings Paints constituents and

    functions

    Protective coatings

    Protecting the surface of an object by the application of coating is a common

    procedure for corrosion protection. A coated surface isolates the underlying metal

    from the corroding environment. The coating applied must be chemically inert and it

    must prevent the penetration of the environment to the material which they protect.

    Pretreatment of metal surface to be plated or coated:

    For proper adhesion of plating or coating the metal surface to be plated should be free

    from greases, oils, rusts and other corrosion products. Removal of theses impurities

    are carried out in the following ways:

    (i) Degreasing:

    Organic solvents such as CCl4, acetone, trichloro-ethylene are used to remove

    oils, greases present on the metal surface.

    (ii) Alkali cleaning:

    This method is used to remove old paint coating. The base metal containing

    old paint coating is removed by keeping it in an alkali cleaning agent. This

    treatment is always to be followed by a thorough rinsing with water.

    (iii) Sand blasting:

    In this method oxide scale present on the steel surface is removed by

    introducing sand into air stream under the pressure o 25-100 atmosphere.

    (iv) Pickling:

    In this process the base metal is immersed in an acid solution. This treatment

    dissolves any corrosion products present on the surface.

    Organic coatings Paints:Paint is a mechanical dispersion mixture of one or more pigments in a vehicle.

    The vehicle is a liquid, consisting of non-volatile, film-forming material, drying oil

    and a highly volatile solvent, thinner. When a paint is applied to a metal surface

    oxidizes forming a dry pigmented film.

    Requisites of a good paint:

    1. It should be fluid enough to spread easily over the protected surface.

    2. It should possess high covering power

    3. It should form a quite tough, uniform, adherent and impervious film

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    4. Its firm should not get cracked on drying.

    5. It should protect the paint surface from corrosion effects of environment.

    6. It should form film and the colour remain quite stable.

    7. Its film should be glossy.

    Constituents of paints:

    A paint essentially consists of the following ingredients

    (i) pigments

    (ii) vehicle or drying oil

    (iii) thinner

    (iv) driers

    (v) fillers or extenders

    (vi) plasticizers and

    (vii) antiskinning agents.

    1. Pigment:

    Pigment is a solid substance, which is an essential constituent of paint. Its

    functions are to (i) provide capacity to paint (ii) provide strength to paint (iii)

    provide desire colour to paint (iv) gives aesthetical appeal to the paint film.

    Examples: Pigments used are whites- white lead, zinc oxide, titanium oxide

    Red red lead, ferric oxide, chrome red

    Blue-Prussian blue,

    Black carbon black

    Brown Brown umbre

    2. Vehicle or drying oil:

    Drying oil is a film-forming constituent of the paint. These are glyceryl esters

    of

    high molecular weight fatty acids, generally present in animal and vegetable oils.

    Functions of drying oil, its a main film forming constituent, acts as a medium,

    gives

    toughness, adhesion, durability and water-proofness.

    Examples: The most widely used drying oil, are linseed oil, soyabean oil and

    dehydrated castor oil.

    3. Thinners:

    It reduces viscosity of the paint, suspend the pigments, increase the elasticity

    of the paint film, help the drying of the paint film as they evaporate.

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    Examples: Turpentine, xylol, kerosene etc.

    4. Driers:

    Driers are oxygen-carrier catalysts. They accelerate the drying of the oil-film

    through oxidation, polymerization and condensation.

    Examples: resonates, linoleates, tungstates and naphthenates of Co,Mn, Pb and

    Zn.

    5. Extenders or fillers:

    It increases durability of the paint, help to reduce the cracking of dry paint

    film.

    Examples: BaSO4, talc, asbestos, china-clay, magnesium silicate, calcium

    sulphate etc.

    6. Plasticizers:

    It provides elasticity to the film and to minimize its cracking.

    Examples: tricresyl phosphate, triphenyl phosphate, tributly phthalate.

    7. Antiskinning agents:

    It prevents gelling and skinning of the paint film.

    Example: polyhydroxy phenols.

    Mechanism in drying of oils:

    The oil film, after it has been applied on the protected surface absorbs oxygen

    at the double bonds, forming peroxides, diperoxides and hydroperoxides which

    isomerise, polymerize and condense to form a characteristic tough, coherent, hard

    elastic, infusible highly cross linked structured macromolecular film.

    Wet paint (oil + pigment + film of oil + pigment pigmented filmextender + drier + thinner) + drier crossed linked

    structure

    Evaporation of thinner oxidation andPolymerization of

    Base material Base material Base material

    Conjugated double bonds

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    Unit - II

    CH2COO(CH2)7-CH=CH-CH2-CH=CH-(CH2)4-CH3

    n CH2COO(CH2)7-CH=CH-CH2-CH=CH-(CH2)4-CH3

    CH2COO(CH2)7-CH=CH-CH2-CH=CH-(CH2)4-CH3

    Glyceride of linolenic acid (drying oil)

    Air oxidationand polymerization

    CH2COO(CH2)7-CH - CH-CH2-CH=CH-(CH2)4-CH3

    O O

    CH2COO(CH2)7-CH - CH-CH2-CH - CH-(CH2)4-CH3

    O O

    CH2COO(CH2)7-CH - CH-CH2-CH - CH-(CH2)4-CH3

    Peroxide crosslink O O

    CH2COO(CH2)7-CH - CH-CH2-CH - CH-(CH2)4-CH3

    O O

    CH2COO(CH2)7-CH - CH-CH2-CH - CH-(CH2)4-CH3

    O O

    CH2COO(CH2)7-CH - CH-CH2-CH - CH-(CH2)4-CH3

    O O

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    Unit - II

    Lecture Session No: 17 Topic: Metallic coatings Principle and methods of

    electroplating, electroplating (Au)

    Metallic coatings Principle and methods of electroplating

    Principle of Electroplating:

    This process involves coating of a thin layer of one metal over another metal

    by passing direct current through an electrolytic solution. The base metal to be plated

    is made of cathode whereas the anode is made of either coating metal itself or an inert

    material in the electrolytic cell.

    Procedure:

    The article to be electroplated is first treated with organic solvent to remove oils,

    greases etc. then, it is made free from surface scales, oxides, etc., by treating with dil.

    HCl or H2SO4. The cleaned article is then made cathode of an electrolytic cell. The

    anode is either the coating metal itself or an inert material of good electrical

    conductivity. The electrolyte is a solution of a soluble salt of the coating metal. The

    electrolytic solution is kept in an electroplating tank. The anode and cathode are

    dipped in the electrolytic solution. When direct current is passed, coating-metal ions

    migrate to the cathode and get deposited there. Thus, a thin layer of coating-metal is

    obtained on the article, made as the cathode. For brighter and smooth deposits,

    favourable conditions such as low temperature, medium current-density and low

    metal-ion concentration are used.

    Electrolyte to ( + ) (-)replenish the loss

    Direct current source

    Cathode

    Anode

    Electroplating

    Factors affecting the electrodeposit:

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    1. Cleaning of the article to be plated: Pretreatment of the surface of any material to

    be electroplated is essential. Maximum coating adhesion can be obtained only, if the

    base metal surface is free from dirt and grease.

    2. pH of the bath liquid: For a good electrodeposit the pH of the bath must be properly

    maintained.

    3. Thickness: For decorative purposes, thin deposit is done, while for corrosion

    resistance, thick plating is required.

    4. Composition of the electrolytic bath: Low metal ion concentrations re preferred,

    since they give rise to very adherent coating films.

    5. Throwing power: Throwing power is the ability of electrolytic cell to give a deposit

    of uniform thickness over the entire cathodic area. When the cathode is regular in

    shape maximum throwing power is exhibited by an electrolytic system

    6. Temperature: Most of the electroplating bath solutions should be used at room

    temperature. However, warm baths are also used to increase the solubility of

    electrolyte thereby increases the concentration and current density of the bath.

    Electroplating of gold:

    Gold plating is a method of depositing of thin layer of gold on the surface of other

    metals, most such as copper or silver. Copper or silver is first electroplated with a

    suitable barrier metal like Sn, Ni or bronze to provide leveling and brightening to the

    substrate and to inhibit the migration of copper or silver into the gold layer.

    Process: The electroplating of gold is carried out by using either neutral cyanide bath

    or acid cyanide bath.

    Anode: inert metal

    Cathode:Cu or Ag or Cd.

    Electrolyte: Gold potassium cyanide K[Au(CN)2]

    Temperature: 70-80C

    pH= 6-8

    Current density : 1-40 mA/cm2

    Additives / Salts /Acids: Citrate, phosphate, phosphoric acid.

    Mechanism: During electrolysis, the electrolyte is decomposed into Au+ ions.

    K[Au(CN)2] K+

    + [Au(CN)2]-

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    [Au(CN)2]- Au+ + 2 CN-

    At cathode, deposition of Au+ occurs

    Au+ + e- Au

    Applications : Gold plating is often used in electronic industries for making printed

    circuit boards, semiconductor lead-out connection because of high electrical

    conductivity (ii) gold plating of silver is used in the manufacture of jewelry.

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    Lecture Session No: 18 Topic: Principle and methods of electroless plating

    ,electroless (Ni) plating

    Electroless plating:

    The process of producing a thin, uniform and hard deposit of metal on an

    activated substrate (Metal or non-metal) by using suitable soluble reducing agents

    without any electrical energy, and the driving force for the deposition is auto catalytic

    redox reactions. The reducing agent reduces the metallic ions to metal, which gets

    plated over the catalytically activated surface giving a uniform thin coating.

    Metal ions + Reducing agent Metal + Oxidised products

    The process involves

    1. Pretreatment or activation of work piece to be plated.

    2. Preparation of bath composition.

    1. Pretreatment or activation of work piece to be plate:

    (i) Metals like Cu, Ag etc. are known as non-catalytic metals. Surface of such

    metals need activation. They are activated by using steel or iron pieces for

    initiating the reactions.

    (ii) Non-metals like glasses, ceramic, plastics are activated by dipping in SnCl,PdCl2 in HCl. This process produces a thin film of palladium coating on non-

    metal surfaces which in turn causes the work piece to get activate for electroless

    plating.

    2. Preparation of bath composition:

    Name of the ingredient Function Examples

    Coating metal ion To provide metal ion for

    deposition

    NiCl2, NiSO4, CuSO4 etc.

    Reducing agent To liberate electrons for

    the reduction of metal ion

    Sodium hypophosphite,

    sodium boron hydride

    Buffer To maintain pH Sodium acetate, NaOH,

    Roschelle salt

    Complexant To improve the quality of

    deposit.

    Sodium acetate, sodium

    citrate

    Exaltant To increase the rate of

    deposition

    Succinate, Maleate,

    Lactate

    Stabilizer to prevent decomposition

    of the plating bath

    Cations like Pb, Ca etc.,

    Brightener To improve the brightness

    of the deposit

    Thiourea, Sodium

    benzoate

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    Electroless plating of nickel:

    1.Pretreatment and activation of surface:

    The surface to be plated is first degreased by using organic solvents or alkali,

    followed by acid treatment.

    Example (i) The surface of the stainless steel is activated by dipping in hot solution of

    50% dil H2SO4

    (ii) Metals and alloys of Aluminum, copper, Iron etc., can be directly Nickel plated

    without activation.

    2.Preparation of plating bath composition

    NiCl2,.6H2O 20g/l - coating solution

    NaH2PO2H2O 20 g/l - reducing agent(Sodium hypophosphite)

    Sodium acetate 10 g/l - Buffer

    Sodium succinate 15 g/l - complexing agent

    Temp 85-95C

    pH 4-6

    Mechanism:

    The pretreated object is immersed in the plating bath for the required time.

    At Anode:

    The reducing agent, NaH2PO2 in solution, moves toward the activated

    substrate and liberates electrons by anodic oxidation.

    H2PO2- + H2O H2PO3

    - + 2 H+ + 2e-

    At Cathode:

    The salt solution containing Ni2+ ions gain electrons and get deposited

    Ni2++ 2e- Ni

    The over all reaction at the surface of work piece is

    Ni2+ + H2PO2- + H2O Ni + H2PO3

    - + 2 H+

    Condition during Electroless plating:

    (a) During the redox reaction, both Ni ions and sodium hypophosphite are

    consumed, so these are replenished periodically.

    (b) Maximum plating obtained at 93C, still higher temperature may cause the

    decomposition of the bath.

    (c) H+ ions are liberated in the redox reaction so pH of the bath solution decrease

    during the process, so addition of buffer is essential to get quality plating.

    Advantages of electroless nickel plating:

    1. It gives rise to harder surface with better wear resistance due to platingof Ni-P alloy.

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    2. Free from pores and possess better corrosion resistance property.

    3. Due to excellent throwing power the object having intricate part with

    irregular shapes can be plated.

    Applications:

    1. Electroless Ni-P coatings are used in various electronic applications.

    2. Electroless nickel deposition on polymers find preferred decorative as well

    as functional applications.

    3. Heat treated electroless nickel coatings finds applications in hydraulic

    compressors, pressure vessels, pumps and fuel injection assemblies.

    4. Plastic cabinets coated with copper and nickel finds applications in digital

    as well as electronic instruments.

    Advantages of electroless plating:

    1. Does not require electrical power source.

    2. It has better throwing power.

    3. Intricate parts with irregular shapes can be uniformly coated.

    4. By adding complexes and additive agents the quality of electroless deposit

    can be improved.

    5. Electroless deposit is less porous hence it gives better chemical,

    mechanical and magnetic properties.

    References:

    (a) Engineering Chemistry, Jain and Jain, Dhanpat Rai Publishing Co., 15th

    Edition.

    (b) Engineering Chemsitry, B. Sivasankar, Tata McGraw Hill Co.,

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