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9Paints, Varnishes,
and Related Products
K. F. Lin
1. RELATIONSHIP OF FATS AND OILSTO THE PAINT-COATING INDUSTRY
Historically, drying oils have been the major film formers of coatings, including
paints, varnishes, and inks. Although it is not certain whether linseed oil was
used in paints in ancient Egypt, flax was grown and flax seeds were collected at
that time. The early Renaissance was probably the real beginning of paints as we
know them today in the West. The Van Eyck brothers (1388–1441) are said to be
the first to use linseed oil as a binder (1). Whereas in China, tung oil has been used
for centuries as waterproofing caulking or as coating for wood objects including
boats, houses, and furniture.
The first American paint factory was opened in Boston in 1737 by Thomas
Childs (2). The pigment and oil were placed on a granite trough, and a granite
ball, known as the Boston Stone, was then rolled over the mixture to make the paint.
The ball is now preserved and serves as the symbol for the Federation of Societies
for Paint Technology.
The drying oils owe their value as raw materials for decorative and protective
coatings to their ability to polymerize and cross-link, or ‘‘dry,’’ after they have been
applied to a surface, to form tough, adherent, impervious, and abrasion-resistant
Bailey’s Industrial Oil and Fat Products, Sixth Edition, Six Volume Set.Edited by Fereidoon Shahidi. Copyright # 2005 John Wiley & Sons, Inc.
307
films. Their film-forming properties are closely related to their degree of unsatura-
tion, since it is through the unsaturated centers or double bonds that polymerization
and cross-linking take place. With one exception (to be noted later) the oils used
in paints varnishes and similar products are relatively high in iodine value. In any
given product, there is an optimum degree of reactivity in the oil; the speed with
which the oil dries must be balanced against such factors as elasticity and durability
in the paint film. In general, however, unsaturation is at a premium in paint and
varnish oils, and the oils in greatest demand are those in which drying takes place
most readily.
The form in which drying oils are used in coating applications has gone
through an evolutionary change over time. The simplest and most primitive
way is to use them directly as the film former of a coating. It was discovered that
drying oils may be made more useful by altering their natural state. By aging
in vats, by heating, or by blowing air through, the viscosity and drying character-
istics of the drying oil may be changed enough to improve its general properties for
coating applications. In the case of fast-drying oils with conjugated double bonds,
such as tung, oiticica, and dehydrated castor oil, heat treatment is necessary to
‘‘gas-proof’’ them, so that the oils do not dry into undesirable wrinked and/or
frosted films. The oils are not necessarily used in their original form of triglycerides
for coating applications. It has become a common practice to hydrolyze them first,
and the free fatty acids are then used to synthesize coating resins with certain advan-
tages. Therefore, the term fats and oils includes fatty acids for the purpose of the
discussions in this Chapter, unless otherwise specified. Through progress, people
found that sometimes mixtures of different oils could be used to greater advantage
and that natural gums could be added; thus oleoresinous varnishes were born.
Thereafter, human creativity started to make rapid and diversed progress in the
development of new coating materials, many of which have departed completely
away from the drying oil base.
When the drying characteristics of oils were relied on as the sole (or major) cause
for a varnish-based coating film to dry, those oils belonging to the linolenic or con-
jugated acid groups, such as linseed, perilla, tung, oiticica, and highly unsaturated
winterized fish oils were of the prime interest to coating formulators. Since about
the 1950s, with the advent of synthetic resins, particularly, alkyd resins, it has
become possible to make considerable use of oils with poorer drying character-
istics. Semidrying oils such as soybean oil, safflower oil, and sunflower seed oil
have become viable as raw materials for making ‘‘drying’’ paints. Nondrying oils,
such as coconut oil, are also used in coating materials. However, their function is
primarily that of a plasticizer rather than of an active component for air drying. In
addition, castor oil, a nondrying oil, has been converted chemically by dehydration
to give excellent drying property.
There is no denying that the once prominent position of fats and oils as the most
important raw material for coatings has been greatly eroded by other materials. The
total U.S. consumption of drying and semidrying oils in coating and allied applica-
tions peaked around 1950 at about 1.2 billion lb. It went down steadily thereafter.
According to SRI International (3), the direct use of drying oils accounted for only
308 PAINTS, VARNISHES, AND RELATED PRODUCTS
about 4% of the total film formers consumed in the United States in 1990, at about
98 million lb, whereas the consumption of alkyds, urethane alkyds, and epoxy esters
was estimated at 645, 40, and 12 million lb, respectively (4–6). Very little drying oil
is used in paints at present. Drying oils and oxidizing alkyds have been studied as
binders for organic inorganic coatings (4). Urethane coatings are the fastest growing
sector. Use in 2003 was 1:6� 106t (5). Epoxy resins are among the most widely
used (6).
2. A BRIEF OVERVIEW OF THE COATINGS TECHNOLOGY
Modern requirements in protective coatings are extremely diverse and exacting.
They go far beyond the mere necessity of protecting the finished surface from
weather or from ordinary wear or abrasion. Some coatings (e.g., those employed
as electrical insulation) must possess extreme resistance to high temperatures or
to penetration by moisture. Others (e.g., marine varnishes and the enamels for coat-
ing the interior of cans) must withstand prolonged contact with water or aqueous
solutions. Modern assembly-line methods of manufacture produce many particular
requirements and have created a special demand for quick-drying finishes. The wide
distribution of illustrated journals, the proliferation of advertising matter, and the
development of high speed printing processes have greatly elaborated the require-
ments of users of printing inks. Tung and other conjugated oils are particularly
suitable for manufacture of fast-drying finishes, and for a time, the consumption
of these oils increased significantly in response to more exacting requirements
for specialized finishes. New systems based on epoxy resins, urethane polymers,
silicones, and other synthetic intermediates have greatly decreased dependency on
tung oil, and use has shrunk significantly.
The complex and diversified requirements of modern industry have to a large
extent removed the manufacture of paints and varnishes from the category of an
art to that of a science. In most plants, the manufacturing processes are now carried
out under careful laboratory control and are freely modified or revised, whenever
revision is indicated, in accordance with known scientific principles. As a result, the
industry has been able to offer a succession of constantly improved products through
periods of fluctuation in the availability of many important raw materials, pressures
for solvent replacement to meet emerging air quality standards, and extensive pig-
ment reformulation to replace mercury and lead to conform to new federal regu-
lations on toxicity.
A most important development in the modern paint and varnish industry has
been the introduction of synthetic resins as replacements for natural resins in the
manufacture of varnishes and enamels. By using synthetic resins it has been pos-
sible to produce a variety of coatings that, in many cases, have important points
of superiority over any of those compounded from natural resins. The synthetic
vehicles are particularly distinguished by their hardness and durability and their
high degree of resistance to the action of water, alkalies, and other chemical
agents.
A BRIEF OVERVIEW OF THE COATINGS TECHNOLOGY 309
New methods for application of paint films and new procedures for curing have
placed challenging demands on the resourcefulness of the resin chemist. For years
brushing was virtually the only method of application; later, spraying, was used.
Now a host of new application and curing techniques are commonplace. These
include roller coating, dipping, coil coating, powder coating, electrodeposition, hot
spray, fluid bed coating, electrostatic spray, two-component spray, ultraviolet
cure, and electron beam cure.
The two foremost reasons for the decline of the direct use of oils, including
oleoresinous varnishes, for coating applications are performance and environment.
Drying oils by themselves, or even in the form of oleoresinous varnishes, do not
give the drying speed and, sometimes, film properties that would satisfy the modern
needs. The ease in the application and cleaning of latex paints caused oil-based
paint to lose most, if not all, of the trade-sales market. The implementation of
Rule 66 in California was the opening salvo for protecting the environment against
solvent-based coatings of which practically all oil-based coatings belong. Thus the
emphasis has switched to the development and commercialization of other coating
materials or systems that are more environment friendly than oil-based materials.
Indeed, it is quite remarkable that in the face of such severe odds, oil-based mater-
ials have been able to hold ground as well as they have.
There is an extraordinary body of terms used to define various features of pro-
tective coatings. Before discussing paints and varnishes and the particular function
of fats and oils in coatings, it is desirable to review and define some of the language
of the industry.
Protective coatings protect (or decorate) surfaces. Greases, mineral oils, plastic
web coats, and mastic compositions may be used for protection, particularly of
metal surfaces; but in the usual sense, protective coatings are materials that form
durable films adhered to the surface to provide protection.
A varnish is a solvent-thinned combination of a drying oil and a hard resin. Also,
a varnish is the clear film obtained using a varnish as a coating vehicle. By exten-
sion, vehicles used for clear films are called varnishes although the vehicle may be a
true varnish, an alkyd resin solution, a urethane-modified oil, or even a lacquer.
A paint is a pigmented system applied to hide and protect a surface. Paints con-
tain a wide range of ingredients as follows:
The vehicle is the carrier for pigment, consisting of combinations of oils, resins,
polymers, and solvents; the nonvolatile portion is commonly called the binder.
Prime pigments are used for their ability to hide or cover the surface. The term
hiding power is used to describe the relative ability of fixed amounts of
different pigments to cover a surface and depends on the difference in
refractive indices between the pigment and the binder; thus primary pigments
usually have high values in refractive index.
Extender pigments give relatively little hiding, but their cost is lower than that of
prime pigments; they provide control of such properties as flow consistency,
durability, and adhesion.
310 PAINTS, VARNISHES, AND RELATED PRODUCTS
Driers are metal salts, especially of cobalt, manganese, zirconium, calcium, and
iron, that accelerate the conversion of the liquid film to a solid; lead was
commonly used as a primary drier, but due to its toxicity, it is rarely used
now.
Solvents or thinners control paint consistency and application properties. Slow
solvents evaporate slowly and leave the film ‘‘open’’ (workable) for longer
periods than fast solvents, which evaporate rapidly; in water-thinned paints,
water is the thinner and there is no control over rate of evaporation.
A variety of other materials may be added for special effects.
Antiskin agents minimize skin formation on the top of the can during use or
storage.
Mildewcides protect the applied film from fungus growth.
Wetting agents or griding aids promote wetting of pigment particles by the
vehicle.
Antiflood and antifloat agents minimize flooding and floating, deficiencies
characterized by separation of colored pigments during drying.
Antisetting agents minimize separation of pigment into a firm or hard mass in
the bottom of the can.
Antisag agents minimize sagging or ‘‘curtaining’’ of wet films during application.
Puffing agents, or thixotropic agents, increase the paint consistency and mini-
mize sagging by giving a thixotropic consistency to paint (a type of behavior
in which the viscosity of the system decreases when agitated, as under the
shear of brushing, and increases when allowed to stand).
Paints are made by grinding pigments in the vehicle. Actually the term grinding
is somewhat inaccurate. The pigments are received from the manufacturer are
already as fine in particle size as they will be in the finished paint. The grinding
operation is designed to break up the aggregates of pigment particles and to dis-
perse them in the vehicle so that each particle is wetted. Griding is usually carried
out in roller mills, in which shear between steel rollers disperses pigments, in ball
mills or pebble mills, in which steel balls or pebbles rotating and rubbing against
each other in a closed cylinder to produce the shear for dispersing the pigment, or in
sand mills, in which agitation of sand causes pigment separation and dispersion. For
products in which a fine grind (fine pigment dispersion) is not required, as in barn
paints or house paints, high speed rotors may be used to grind the paint. In typical
paint manufacture, a paste prepared from all of the pigment and a portion of the
vehicle is subjected to the appropriate grinding technique until the desired fineness
of grind is attained, and the resultant paste is ‘‘let down’’ (diluted) with the remain-
ing portion of vehicle and solvent.
Fineness of grind is commonly expressed numerically using a grind gauge,
which is a shallow wedge cut from polished metal. Paint is filled into the wedge
A BRIEF OVERVIEW OF THE COATINGS TECHNOLOGY 311
and a bar is drawn across the surface. With fine grinds, the paint fills the wedge even
to the shallowest part. With coarse grinds, the paint is pulled away from the shallow
edge of the wedge of the deeper end. The line of demarcation ranging from 0
(very coarse grind) to 8 (ultrafine grind) designated the quality of the pigment
dispersion.
An enamel is a paint based on a vehicle that dries to a considerably harder film
than paints derived from unmodified drying oils. Paints and enamels are classified
by type of finish as follows:
Flat paints or enamels dry to a velvety nonglossy or matte surface.
Semigloss paints or enamels dry to an intermediate gloss range between flat and
glossy.
Gloss paints or enamels dry to a highly reflecting surface.
There are many variations in the nomenclature, and films that are called gloss
films by one observer might be classified as a semigloss by the individual who
demands mirrorlike surfaces. Other designations might be used also such as egg-
shell (between flat and semigloss) or full gloss to differentiate mirror gloss from
normal gloss.
The degree of gloss is measured by a glossmeter, which measures light reflec-
tance at a low angle from the horizontal (20� gloss) or high angle (60� gloss). The
60� reflectance is most common, and although ranges of values are not sharply
divided, the general consensus is as follows:
Since the ability of a surface to reflect light, which gives the gloss measurement,
depends on the smoothness of the surface, one can readily visualize that a coating
with a greater surplus of binder over its pigment content will have a greater ability
to produce a smooth surface, thus high in gloss. Conversely, with a high pigment
content, there will be more pigment particles or aggregates at or near the film sur-
face to cause a scattering of light, thus resulting in low gloss. The amount of pig-
ment in the paint is measured by the pigment volume concentration (PVC), i.e., the
volume percent of pigments in the dried paint film. In solvent-based systems,
products of low PVC (up to 20–25%) are glossy, products in the middle range
Type of Paint 60� Reflectance
Flat 4 or 5 maximum
Eggshell 5–20
Semigloss 20–60 (up to 80)
Low gloss 80 to 90þHigh or full gloss 90 to 98þ
312 PAINTS, VARNISHES, AND RELATED PRODUCTS
(25–50%) have a semigloss finish, and products in the high range (45–70) have a
flat or matte surface. Gloss in water-thinned systems does not correspond to the
above, particularly in emulsion systems, because the pigment particles are not
wetted uniformly by the binder. Solvent-thinned paints containing certain ‘‘flatting
agents’’ such as extremely fine silica do not conform to the normal pattern.
Coating systems are divided into two general classifications, depending on the
point of application. Trade sales finishes are purchased by the user in a paint store
or hardware store (or today even in a drugstore or a supermarket) and are applied by
the purchaser, usually by brush or roller. Included are barn paints, house paints, trim
paints, varnishes, porch and deck enamels; wall paints, architectural enamels, and
similar user-applied finishes. Industrial finishes are applied to objects by the manu-
facturer, usually by spraying, dipping, roller coating, air knife, or other high speed
production application methods, and they are usually force dried by baking. Imple-
ment, automotive, appliance, and furniture finishes are typical industrials.
Finishes are also described by the function of the paint. A primer is used to coat
the original surface. Its major functional property is good adhesion. Protection
against corrosion is an especially important characteristic of metal primers. Hiding
is a secondary function.
A sealer is a primer whose major function is covering a porous surface such as
plaster, gypsum board, or paperboard with a surface coating that exhibits a mini-
mum penetration into the surface. Good sealing prevents ‘‘ghosting,’’ a film defect
in which variation in penetration causes gloss differences and visual color differ-
ences in the final coat. A typical ghosting effect is obtained in painting wallpaper
in which the pattern can show through multiple coats because of the variability in
porosity of the substrate.
A sanding sealer is designed for easy sanding after short dry so that smoother top
coats can be attained. Sanding sealers are most important in furniture finishes and
industrial finishes such as automotive systems.
An undercoat is another name for primer or sealer, especially as an enamel
undercoat, which serves to supply a uniform base for an enamel so that there
will not be a wide variation in gloss. Undercoats may be applied over sealers.
The top coat or finish coat is the outside layer of paint applied over the primer
or sealer.
The specification of products for coating applications involves a large number of
factors, including color and color retention of films, rate of setup, bakability, rate of
cure of films, hardness of films, adhesion, wetting action in grinding with pigments,
flexibility and retention of flexibility on aging, reactivity with pigments, reactivity
with driers, water resistance, alkali resistance, solvent resistance, viscosity, visco-
sity stability in the package as clear products or in pigmented systems, thermo-
plasticity, durability, compatibility with other film-forming agents, mar resistance,
abrasion resistance, stain resistance, performance in the varnish kettle, gloss, gloss
retention, etc. Obviously, no single product can be optimum in all of these character-
istics, and in each use a compromise must be made to provide the best performance
in the intended usage.
A BRIEF OVERVIEW OF THE COATINGS TECHNOLOGY 313
3. FILM DRYING PROCESS OF OIL-BASEDCOATING MATERIALS
3.1. Drying of a Nonconjugated System
As mentioned earlier, it is through the unsaturated centers or double bonds of the
fatty acids in drying oils that polymerization and cross-linking, i.e., drying, takes
place. Hence, oils are conventionally classified, based on their iodine values into
three groups: drying, semidrying, and nondrying. The generally accepted demarca-
tions are, respectively, >140, 140–125, and <125. These numbers are, more or less,
arbitrarily assigned. When the oil contains conjugated double bonds, the iodine
values determined are usually low due to incomplete halogen absorption. Such a
classification can only be used for a rough guidance.
Wicks and Jones (7) suggested that the methylene groups between two double
bonds, i.e., the CH2 groups allylic to two C����C groups, are much more reactive than
those being allylic to only one C����C group and are mostly responsible for the dry-
ing of the nonconjugated oil. Thus the average number of such groups fn in an oil
molecule serves as a better indicator for the drying characteristics of the oil. An oil
with an fn value of greater than 2.2 is a drying oil, those with fn values somewhat
less than 2.2 are semidrying, and there is no sharp dividing composition between
semidrying and nondrying oils, according to the authors. While such a classification
system does have merits over the conventional way (based on iodine value), it does
not provide a ‘‘rule’’ for classifying oils with conjugated unsaturation.
The chemical mechanism of drying has been established as an oxidative radical
chain reaction process, which has been summarized as follows (8):
1. A period of induction at the beginning of the reaction during which no visible
change in physical or chemical properties in the oil is noticed; natural
antioxidant compounds are consumed during this period.
2. The reaction becomes perceptible and oxygen uptake is considerable; discrete
interaction of oxygen and olefins takes place followed by the formation of
hydroperoxides.
3. Conjugation of double bonds occurs accompanied by isomerization of cis to
trans unsaturation.
4. The hydroperoxides start to decompose to form a high free-radical concen-
tration; the reaction becomes autocatalytic.
5. Polymerization and scission reactions begin and yield high molecular weight
cross-linked products and low molecular weight carbonyl and hydroxy
compounds; carbon dioxide and water are also formed and are present in
the volatile products of film formation.
It is now generally believed that the induction is slow at first but is autocatalytic
and the rate increases steadily. The rate depends on the reaction conditions such as
temperature, light, and traces of heavy metals or inhibitors in the oil or coating (9).
314 PAINTS, VARNISHES, AND RELATED PRODUCTS
The active sites are the allylic carbon a to a double bond, especially those a to
two double bonds with one on each side, such as carbon number 11 in a 9,12-octa-
decadienoic (linoleic) acid and proceeds through the following mechanism:
CH CH CH2 CH CH
−H
CH CH CH CH CHCH CH CH CH CHCH CH CH CH CH
O2
CH CH CH CH CH
OO
CH CH CH CH CH
OO
CH CH CH CH CH
OO
H
CH CH CH CH CH
OOH
CH CH CH CH CH
OOH
CH CH CH CH CH
OOH
Abstraction of a hydrogen atom
Resonance hybrid free radicals
Three possible peroxy radicals
Addition of hydrogen atom abstractedfrom another linoleate molecule
Three possible hydroperoxides, two ofwhich are conjugated
The initial step is believed to be the dehydrogenation from the a-methylene group
to form a radical. Since such a hydrogen extraction would require a considerable
amount of energy, a number of investigators proposed that the hydrogen is removed
through reaction with a free radical. Thus a radical, A � , abstracts a hydrogen from a
molecule of linoleate, RH, to form the radical R � ,
RHþ A� ! R � þAH
Since the radical is allylic to the double bonds on either side of it, resonance hybrid
free radicals are formed resulting in shifting the double bonds to a conjugated posi-
tion. This is then followed by:
R � þO2 ! RO2�
FILM DRYING PROCESS OF OIL-BASED COATING MATERIALS 315
and
RO2 � þRH! ROOHþ R�
The net reaction is hydroperoxide formation:
RHþ O2 ! ROOH
During the oxidation to form hydroperoxides, the natural cis,cis unsaturation of
linoleate is converted to cis, trans and trans, trans isomers. Privett and co-workers
(10) concluded that at least 90% of linoleate hydroperoxide preparations are conju-
gated. When the oxidation is conducted at 0�C the hydroperoxides are predomi-
nately cis, trans isomers, but room temperature oxidation produces a large
amount of trans, trans unsaturation (11, 12). Ethyl or methyl linoleate hydroperox-
ides are relatively low melting and as a result purification by crystallization is dif-
ficult. Bailey and Barlow (13) prepared high melting p-phenylphenacyl linoleate,
oxidized the ester in benzene solution, and isolated virtually pure hydroperoxide
by crystallization. Infrared spectra of the 99% purity p-phenylphenacyl linoleate
hydroperoxide correspond to a trans, trans conjugated isomer.
The autoxidation of linoleate described above shows the characteristic features
of a chain reaction involving free radicals. Materials that decompose to form free
radicals catalyze the reaction even when present in very low concentrations to
produce high yields of hydroperoxides; initiation of the reaction by light can pro-
duce quantum yields much greater than unity and easily oxidized substances that
consume free radicals, but do not themselves undergo significant autoxidation,
can markedly inhibit the chain reaction.
Although there is quite general agreement on the mechanism of the chain pro-
pagation reaction, there is much less unanimity of opinion on the primary reaction
to produce the radicals (indicated as A � above) responsible for the initiation of the
chain reaction. Originally, it was proposed that hydroperoxides are the initial pro-
ducts of autoxidation (14, 15). Primarily because of the high energy requirement for
rupture of the a-methylenic carbon–hydrogen bond several authors (16–19) almost
simultaneously concluded that the initial point of oxidative attack was the double
bond and not the a-methylene group, although some (16) proposed a limited attack
at the double bond to produce radicals in sufficient amount to initiate the chain reac-
tion through the a-methylenic carbon.
Kahn (20) questioned the formation of a diradical and proposed direct addition
of oxygen to a double bond to form a cyclic transition state, which breaks down
to yield the hydroperoxide. The theory of oxidation has received little support,
because it does not explain the inhibitory effect of free-radical acceptors in the ini-
tial stages of autoxidation.
It has been contended that the direct attack of oxygen on the double bond has
low thermodynamic probability (21, 22), and it has been considered that trace metal
contaminants catalyze the initiation of autoxidation by producing free radicals
through electron transfer. Alternative pathways are as follows, using cobalt as an
316 PAINTS, VARNISHES, AND RELATED PRODUCTS
example of a metal that can facilely shift valence states in oxidation–reduction
reactions:
1. Reduction activation of trace hydroperoxides in the system yields free
radicals.
Co2þ þ ROOH! Co3þ þ OH� þ RO�
2. Direct reaction of a metal ion with oxygen:
Co2þ þ O2 ! Co3þ þ O�2 �
The O�2 � radical ion reacts readily with a proton to form the HO2� radical,
which can initiate the chain reaction of oxidation.
3. Complex reaction of metal compounds with oxygen and subsequent forma-
tion of an HO2� radical.
Co2þ þ O�2 ! Co3þ � O2
Co3þ � O2 þ XH! Co3þ þ X� þ HO2�
4. Oxidation by electron transfer of the a-methylenic group by the metal ion.
Co3þ þ RH! Co2þ þ Hþ þ R�
According to Uri (21) the kinetic and thermodynamic probabilities for formation of
free radicals by the metal-catalyzed initiation reaction are considerably more favor-
able than the Bolland and Gee (16) proposal of diradicals by direct oxidation of a
double bond.
Once hydroperoxides are formed, even in trace amounts, they can play a
profound role in the autocatalysis. Monomolecular decomposition yields two free
radicals:
ROOH RO HO+
A bimolecular reaction, perhaps proceeding through intermediate hydrogen bond-
ing, is more probable:
ROO H
HOOR [ROO H
HOOR] HOH RO RO2+ + +
Either the monomolecular or the dimolecular decomposition serves to feed new
radicals into the reaction to initiate the chain reaction of autoxidation. These radicals
may further react through different paths. They may follow a radical chain mechan-
ism or other well-known radical reactions, such as coupling or disproportionation.
FILM DRYING PROCESS OF OIL-BASED COATING MATERIALS 317
The reactions may lead to the formation of dimers or polymers or may achieve
cross-linking, resulting in an insoluble, infusible film (i.e., drying). Apparently,
the dominant reaction path depends on the temperature. At room temperature,
mostly C��O��C bonds are produced, whereas C��C bonds are predominantly
formed under baking conditions.
The free radicals may also undergo chain cleavage reactions. Low molecular
weight by-products, such as water, carbon dioxide, aldehydes, ketones, and alcohols
may be formed, which cause the odor and taste of the oils. The strong odor of
rancid soybean oil was shown to be caused by 2-pentylfuran found in oxidized oil
in storage (23).
Chemically, the air-drying of a nonconjugated oil such as linseed is character-
ized by the adsorption of 12–16% by weight of oxygen. The reactivity of drying
oils is based on the mesomeric stabilization of the radical intermediate: the un-
paired electron is delocalized over several carbon atoms, and less energy is required
to eliminate the proton as illustrated below (24).
3.2. Drying of a Conjugated System
Tung oil, whose dominant feature is the conjugated cis, trans, trans-9,11,13-octa-
decatrienoic acid, a-eleostearic acid, dries to a coherent film with absorption of
only 5% by weight of oxygen. Privett (25) suggested oxidation through 1,2- or
1,4-addition to the diene system to yield noncyclic peroxides. Faulkner (26) iden-
tified 1,6-peroxide in addition and suggested that the autoxidation does not proceed
via hydroperoxide groups but rather via cyclic peroxides. It has also been found that
the triene content decreased and the diene content increased in proportion to the
absorption of oxygen (27, 28). The main reaction is believed to consist of a direct
attack by oxygen on the C����C double bonds to form cyclic peroxides and dienes.
The peroxides then react with allylic methylene groups or thermally dissociate to
give radicals, initiating a radical chain reaction mechanism, forming polymers via
C��C or C��O��C bonds (29).
4. OLEORESINOUS VARNISHES
As noted, coating systems were advanced from oil-only vehicles to oleoresinous
varnishes for improved performances. These are basically oils that have been
Activation Energy Relative Rate
Triglycerides Mesomers (kJ/mol) of Oxidation
Stearate a 415 0
Oleate 2 335 1
Linoleate 5 289 120
Linolenate 11 168 330
aSaturated molecules.
318 PAINTS, VARNISHES, AND RELATED PRODUCTS
‘‘hardened’’ or modified by treatment with one or more suitable resins, natural
or synthetic. The oils and resins are combined, usually by heating together
at temperatures of 250�C or above, until a homogeneous mixture is formed. In
most cases, it is simply a case of dissolving the resin or resins in the oil. In
some cases, chemical reaction may have taken place between the resin and the
oil, such as that between the methylol groups of a ‘‘heat-reactive’’ phenolic resin
and the double bonds of a drying oil in forming a chroman ring structure as shown
below (30):
OH
R
CH2OHHOH2C
+
R′CH
CH
R′′
O
C
CHCH
R
R′
H R′′HOH2C
Chroman ring structure
The major improvements obtained by incorporating resins into drying oils are faster
drying, greater film hardness, higher gloss, better water and chemical resistance,
and greater durability. The degree of property change depends on the type and
the amount of the resin incorporated in the oil. Varnish makers express the oil to
resin ratio in terms of oil length, which is defined as the number of gallons of oil
used per 100 lb of the resins in the varnish. Varnishes are categorized according to
their oil length as short- (5–15 gal), medium- (16–30 gal), and long-oil (30þ gal)
varnishes. These demarcations are somewhat arbitrary and not universally agreed.
From oleoresinous varnishes, the coatings industry progressed into alkyd resins.
While one might say that this was only an evolutionary change, it nevertheless did
open a new horizon for coating technologists and has been responsible for the long-
evity of oil-based coating materials. It behooves us to take a more comprehensive
look at the various aspects of alkyd resins.
5. ALKYD RESINS
Alkyd resins have been the workhorse for the coatings industry over the last half
century. The term alkyd was coined to define the reaction product of polyhydric
alcohols and polybasic acids, in other words, polyesters. However, its definition
has been narrowed to include only those polyesters containing monobasic acids,
usually long-chain fatty acids. Thus thermoplastic polyesters typified by polyethy-
lene terephthalate (PET) used in synthetic fibers, films, and plastics and unsaturated
polyesters typified by the condensation product of glycols and unsaturated dibasic
acids (which are widely used in conjunction with vinylic monomers in making
sheet molding compounds or other thermosetting molded plastics) are not consid-
ered as part of the alkyd family and are beyond the scope of the present discussion.
ALKYD RESINS 319
The first appearance of the term alkyd resin in the subject index of Chemical
Abstracts was in 1929, under ‘‘resins.’’ It was not until 1936 that alkyd resins was
listed in its alphabetical place, but still appeared as ‘‘see resinous products.’’ The
proliferation of literature on alkyd resins peaked in the 1940s through the 1960s.
Research activities on alkyds in the United States, as indicated by the number of
publications, has apparently tapered off in the last two decades. Readers who are
alkyd history buffs can find more detailed historical reviews (31–34).
In spite of the challenges from many new coating resins developed over the
decades, alkyd resins, as a family, have maintained a prominent position even until
today. There are two major reasons for such sustained popularity. First, alkyds are
extremely versatile. An alkyd technologist can choose from a large variety of reac-
tion ingredients and at widely different ratios to tailor the structure and properties
of the resin or to obtain similar resin properties from different ingredients, as their
availability or cost may sometimes so dictate. For almost any given coating appli-
cation, from baking enamels for appliances to flat house paints to clear wood
finishes, one can design an alkyd resin to meet the property requirements. The
second reason is that alkyd resins can be made at relatively low cost. Most of
the raw materials are fairly low cost commodity items, and major capital investment
and high processing cost are not needed to produce the resins.
5.1. Basic Reactions and Resin Structure
The main reactions involved in alkyd resin synthesis are polycondensation by ester-
ification and ester interchange. If one uses the following symbols to represent the
basic components of an alkyd resin: O R
O
O , a polyol molecule or radical;
X��A��X, a polybasic acid molecule or radical; and X��F, a mono-basic acid mole-
cule or radical, a schematic representation of the resin molecule can be given (Fig-
ure 1). As Figure 1 implies, there is usually some amount of residual acidity along
with free hydroxyl groups left in the resin molecules. The structure-property rela-
tionship and the principles commonly followed to design the resin structure will be
discussed below.
5.2. Classification of Alkyd Resins
Alkyd resins are usually referred to by a shorthand description based on a certain
way of classification or a combined classification, from which the general properties
Figure 1. Schematic representation of an alkyd resin molecule.
320 PAINTS, VARNISHES, AND RELATED PRODUCTS
of the resin become immediately apparent. The commonly used bases for classi-
fication are as follows.
Drying versus Nondrying, and the Specific Source of Fatty Acids. Alkyd resins
can be broadly classified into the drying type and the nondrying type, depending on
the ability of their film to dry by air oxidation. This drying ability is derived from
the polyunsaturated fatty acids in the resin composition. If drying oils, such as
linseed oil, are the sources of the fatty acids for the alkyd, the resin would belong
to the drying type and is usually used as the film former of coatings or inks. On the
other hand, if the fatty acids come from nondrying oils, such as coconut oil, the
resin would be a nondrying alkyd. They are used either as plasticizers for other
film-formers, such as in nitrocellulose lacquers, or are cross-linked through their
hydroxyl functional groups to become part of the film former. More frequently,
an alkyd resin is classified by the source of the fatty acids, e.g., a linseed alkyd,
a tung oil-modified soy alkyd, and a coconut alkyd.
Classified by Oil Length or Fatty Acid Content. Probably inherited from oleo-
resinous varnish practice but with a different way of expression, alkyd resins are
also classified by their oil length. For an alkyd resin, the oil length is defined as
the weight percent of oil or triglyceride equivalent, or alternatively, as the weight
percent of fatty acids in the finished resin, for example, the resin represented in Fig-
ure 1. The structure indicates that the molar ratio of these three ingredients is
4 : 4 : 3. Assume that the polyol is glycerol, the polybasic acid is phthalic anhydride,
and the fatty acids came from soybean oil with an average molecular weight of 280.
The formula weight of the resin would be 1674 and the triglyceride equivalent of
the fatty acids would be 878, thus the oil length would be 52.4%. Alternatively, the
above resin would be described as one having 50.2% fatty acids. Since the over-
whelming majority of alkyd resins are based on phthalic anhydride, it is also
customary to describe an alkyd in terms of its phthalic anhydride content in per-
cents based on the finished resin.
By this approach, alkyd resins are classified into four classes:
It should be noted that these demarcations are arbitrary and may vary from author to
author. Furthermore, the boundaries are usually not clear-cut.
More frequently, alkyd resins are described by a combined classification in terms
of their oil length, the type of fatty acids, and any unusual ingredients. Such
descriptions as an isophthalic, very long tall oil alkyd or a medium oil dehydrated
castor-PE (the PE refers to pentaerythritol, not polyethylene) alkyd or a short oil
lauric-benzoic alkyd would immediately project the general properties of the resin.
Percent Fatty Percent Phthalic
Resin Class Percent Oil Acids Anhydride
Very long oil >70 >68 <20
Long oil 56–70 53–68 20–30
Medium oil 46–55 43–52 30–35
Short oil <45 <42 >35
ALKYD RESINS 321
5.3. Oil Length–Resin Property Relationship
Obviously, the oil length of an alkyd resin has profound effects on the properties of
the resin. A few of these effects are discussed below.
Effect on Solubility. At long oil lengths, the aliphatic hydrocarbon chains of the
fatty acids constitute the major portion of the mass of the resin molecules; there-
fore, the resin would be soluble in nonpolar aliphatic solvents. Conversely, as the
oil length decreases and the phthalic content increases, the aromaticity of the resin
molecules increases, and the aromaticity and/or the polarity of the solvent will also
need to be increased to dissolve the resin effectively.
Effect on Drying Characteristics. Alkyd resin molecules have a comblike struc-
ture, with a thermoplastic polyester backbone and dangling fatty acid side chains.
Each of these two fractions contributes to the drying, or film-forming, characteris-
tics of the resin. The backbone fraction dries by solvent release, similar to a lacquer
material, whereas the side chain fraction dries in a manner similar to the oil from
which the fatty acids came. Therefore, short oil alkyds develop a surface dryness
relatively quickly due to a faster solvent release, which is often further facilitated
by the fact that the solvents used have high volatility. However, their through-dry in
air is usually slower, because the fatty acid side chains are fewer in numbers and
more scattered in space to cross-link with each other through the action of oxygen,
and the dry surface would impede the transportation of air oxygen to reach down
into the film. On the other hand, long oil alkyds are relatively slow in reaching the
‘‘set-to-touch’’ stage of surface drying, but the greater abundance of fatty acid side
chains and the relative openness of the film surface would facilitate the film to reach
through-dry.
Other trends of changing properties (Table 1) would become obvious, consi-
dering how the structure of resin molecules would change with oil length. Theoreti-
cally, one could design and make alkyd resins at almost any oil length. However, for
any given set of starting ingredients, as the oil length goes up, it will reach a point
TABLE 1 Trends of Property Changes with Oil Length of Alkyd
Resinsa.
Oil Length Long Medium Short
Requirement of aromatic, polar solvents ������������������������������!Compatibility with other film formers ������������������������������!Viscosity ������������������������������!Ease of brushing ����������������������������������������Air dry time, set-to-touch, ��������������������������������������Through-dry ���������������� ���������������!Film hardness ������������������������������!Gloss ������������������������������!Gloss retention ������������������������������!Color retention ������������������������������!Exterior durability ���������������� ���������������!aPrimarily referring to drying-type alkyds.
322 PAINTS, VARNISHES, AND RELATED PRODUCTS
where the maximum extent of fatty acid modification of the polyester molecules has
been achieved, and any additional amounts of fatty acids or oil remain as separate
entities, blended with the polyester molecules. Refer again to the resin structure in
Figure 1. If the molar ratio is 1 : 1 : 1 among glycerol, phthalic anhydride, and soy
acids and the reaction was carried to completion, the resin would have an oil length
of 60.5%, or 57.9% of fatty acids. There is no more room in the resin structure to
accommodate any additional amount of fatty acid. Therefore, with those three
ingredients, if the oil length exceeds 60.5%, the excess amount of oil would only
be retained in the resin as a blend. Obviously, the ‘‘very long oil’’ types of alkyd
resins would almost certainly be resin–oil blends.
The maximum oil length of an alkyd resin (before it becomes a resin–oil blend)
depends on the molecular weight of the ingredients as well as the functionality of
the polyol. If the C18 soy fatty acids in the above example is replaced with C12
lauric acid, the transition would be reached at 52.6% oil. On the other hand, if a
tetra-hydroxyl polyol, such as pentaerythritol, replaces glycerol, the stoichiometry
would allow 2 moles of fatty acids, for every 1 mole of phthalic anhydride and
pentaerythritol. Thus theoretically, the maximum amount of soy fatty acids that
may be chemically combined in the resin structure would be 70.9%, equivalent
to a 74.1% oil length.
5.4. Major Ingredients
Each of the three principal components of alkyd resins—the polybasic acids, the
polyols, and the monobasic acids—has a large variety to be chosen from. The selec-
tion of each one of these ingredients will affect the properties of the resin. As will
be shown later, the choice of ingredients may even affect the choice of manufac-
turing processes. To both the resin manufacturers and the users, the selection of the
proper ingredients is a major decision.
Polybasic Acids and Anhydrides. The major types of polybasic acids used in
alkyd preparation are as follows.
Phthalic anhydride is by far the most important dibasic acid used in alkyd prepara-
tion, because of its low cost and the excellent overall properties it imparts to the
Molecular Equivalent
Type Weight Weight
Phthalic anhydride 148 74
Isophthalic acid 166 83
Maleic anhydride 98 49
Fumaric acid 116 58
Adipic acid 146 73
Azelaic acid 160 80
Sebacic acid 174 87
Chlorendic anhydride 371 185.5
Trimellitic anhydride 192 64
ALKYD RESINS 323
resin. Its anhydride structure allows a fast esterification to form half-esters at rela-
tively low reaction temperatures without liberating water, thereby avoiding the dan-
ger of excessive foaming in the reactor. However, since the two carboxyl groups of
phthalic anhydride are in the ortho position to each other on the benzene ring,
cyclic structure may and does occur in the resin molecules. Consequently, the
development of chain length of the polymer would be restricted, and the average
molecular weight would tend to be low. Phthalic anhydride has a tendency to sub-
lime. (Heat of sublimation: 143 g-cal/g; heat of vaporization: 87.2 g-cal/g.) There-
fore, care must be taken to prevent its loss.
Isophthalic acid is the meta isomer of phthalic acid. Since the two carboxyl
groups are adequately separated, the chances of forming a cyclic structure in the
resin molecules are greatly diminished. Therefore, isophthalic alkyds usually attain
higher molecular weight and show much higher viscosity than their phthalic coun-
terparts at the same oil length. This is the major motivation for resin manufacturers
to use isophthalic acid for the preparation of long oil alkyds. Another major
advantage of isophthalic acid is that the resultant alkyd resins show much higher
thermal stability than the phthalic type (35). In spite of these advantages, isophtha-
lic acid has not gained the same popularity as phthalic anhydride in alkyds, because
the resin making process is much more complicated and difficult than that with
phthalic anhydride. Its melting point (350�C) is much higher than that of phthalic
anhydride (131�C), and it has a low solubility in the initial alkyd reactants, which
causes the reactants to stay as a two-phase solid–liquid system and does not become
clear until the reaction is near complete (36, 37). The diacid does not readily form
half-esters at relatively low reaction temperature as would the anhydride, and twice
as much water will be formed and needs to be removed from esterification. Usually,
additional care and equipment are needed for the higher processing temperature
required for isophthalic acid.
The para isomer terephthalic acid may also be used for making alkyds. The
resultant resins showed even better thermal stability than isophthalic alkyds (35).
However, it has all the disadvantages of isophthalic acid and is more expensive.
It is rarely used in making alkyd resins.
Maleic anhydride is sometimes used for partial substitution of phthalic anhy-
dride in making alkyds. It imparts vinylic unsaturation functionalities in the back-
bone chain of the resin molecules, which allows the resin to be grafted with styrene,
acrylic esters, or other vinyl monomers. The presence of a small amount of maleic
anhydride, up to 10% on molar base of the total dibasic acids, in the resin formula-
tion would accelerate the viscosity increase during the resin manufacturing process.
The resins usually dry more rapidly and give harder films with improved color,
adhesion, water resistance, alkali resistance, and exterior durability. However, the
resin cooking process needs to be monitored and controlled with greater care, parti-
cularly when it is near the desired end point, to prevent gelation. Fumaric acid, the
trans isomer of maleic acid, may be used in an equivalent manner.
Maleic and fumaric acid can also be, and are often, incorporated in alkyd resins
in the form of the Diels-Alder adduct of rosin. The adducts are tribasic acids. They
provide one of the means to impart pendant carboxyl groups in the resin molecules,
324 PAINTS, VARNISHES, AND RELATED PRODUCTS
which can then be saponified to give ionic and, in turn, water-soluble characteristics
to the resin. Alkyds containing maleic–rosin adducts often have poorer color reten-
tion, toughness, gloss retention, and exterior durability.
Aliphatic dibasic acids, such as succinic, adipic, azelaic, and sebacic acids have
also been used to make alkyd resins. Their linear and flexible chain structure lends
higher flexibility and lower viscosity to the resin than the rigid aromatic rings of
phthalic acids.
Chlorendic anhydride is the Diels-Alder adduct of maleic anhydride and hexa-
chlorocyclopentadiene. It is also known as hexachloro-endo-tetrahydrophthalic
(HET) anhydride. The major interest of the alkyd industry in this material is that
the resultant resins contribute to the flame retardancy of the coatings. It has been
reported to give a greater reaction rate than phthalic anhydride, such that at 204–
210�C (400–410�F) the reaction rate approximates that of phthalic anhydride at a
temperature of 238�C (460�F) (38). However, the resins are prone to develop darker
color, particularly at high processing temperature. Tetrachlorophthalic anhydride,
made by conventional chlorination of phthalic anhydride, would also impart flame
retardancy to its alkyds. However, it is appreciably less soluble in the usual proces-
sing solvents than is phthalic anhydride and is reported to be of appreciably lower
chemical reactivity (39).
Trimellitic anhydride (TMA), 1,2,4-benzenetricarboxylic acid anhydride, has
gained greater prominence in recent years due to the greater interest in water-
soluble alkyds. A partial substitution of the phthalic anhydride with TMA gives a
measured quantity of pendent carboxyl groups for water solubilization with
ammonia or other suitable base. The anhydride hydrolyzes to the acid form simply
by allowing it to stand in open containers. Premature cross-linking of alkyd resins
formulated with a high content of TMA would occur at high acid numbers when
large amounts of trimellitic acid are present (40).
Polyhydric Alcohols. The major types of polyol used in alkyd synthesis are as
follows.
Pentaerythritol (PE) is one of the most important polyols used in alkyd resins. Its
molecular structure, four methylol groups (CH2OH) surrounding a center carbon
atom, is the basis for its many interesting attributes. The four equal and highly
Molecular Equivalent
Type Weight Weight
Pentaerythritol 136 34
Glycerol 92 31a
Trimethylolpropane 134 44.7
Trimethylolethane 120 40
Ethylene glycol 62 31
Neopentyl glycol 104 52
aSince glycerol is usually supplied at 99% purity (1%
moisture), its equivalent weight is commonly assumed to
be 31 in recipe calculations.
ALKYD RESINS 325
reactive primary hydroxyl groups make it versatile for designing resin structures,
and the neopentyl core structure lends stability against heat, light, and moisture.
As a result, alkyds based on PE usually are superior to their counterparts based
on glycerol in viscosity, drying properties, film hardness, gloss retention, color
and color stability, humidity resistance, thermal stability, and exterior durability.
On the other hand, its high functionality demands that the resin composition be
more carefully designed and the synthesizing process be more carefully monitored
and controlled to reduce or eliminate the tendency of gelation. Dipentaerythritol
and tripentaerythritol are linear dimer and trimer of PE. They are hexa- and octa-
functional polyols, respectively. Technical grades of PE usually contain small or
trace quantities of di- and tri-PE that were not completely removed in the manufac-
turing process. The high functionality of these materials makes them impractical to
be considered as the sole or major polyol of an alkyd resin.
Among the triols, glycerol is undoubtedly the most important one in alkyd tech-
nology. Natural fats and oils are triglycerides. Therefore, whenever oils are used
directly as the source of fatty acids in an alkyd resin, glycerol will automatically
be a part of the polyols of the resin. Besides the difference in functionality, the
major difference between glycerol and PE is that one of the hydroxyl groups in
glycerol is secondary, which has lower reactivity than primary hydroxyl groups.
This often manifests itself as if glycerol had a de facto functionality of less than
3. Consequently, a larger excess of glycerol would be required in the resin formulas,
which would result in poorer resin properties as a coating material. At high tempe-
ratures, the proton on the secondary carbon in glycerol may undergo a dehydration
reaction with one of the primary hydroxyl groups on the adjacent carbon atom to
give water and acrolein, whereas such reaction is not possible with PE. Glycerol
alkyds are more prone to thermally decompose to give color bodies, resulting in
darkening of the resin.
Trimethylolethane and trimethylolpropane are synthetic triols. Like PE, they
have the neopentyl structure and equivalent primary hydroxyl functional groups.
Therefore, they also yield alkyds with better resistance to heat, light, moisture, and
alkali than glycerol. They have one less hydroxyl group than PE, and the equivalent
weights of these polyols are higher than that of PE. Trimethylolethane has been
reported to give alkyds that are faster drying and higher in film hardness than tri-
methylolpropane (41), whereas trimethylolpropane was claimed to give alkyds with
better water and alkaline resistance, color and color retention, and impact resistance
than trimethylolethane (42).
Diols such as ethylene glycol, propylene glycol, and neopentyl glycol are some-
times used as part of the polyols in alkyd formulations primarily for the purpose of
regulating the functionality of the reaction system. Their relatively low boiling
points, (197, 188, and 207�C), respectively, for the above three glycols) require that
special precautionary measures be taken during the resin manufacturing process.
Analogous to the use of linear a,o-dibasic acids (such as adipic and sebacic),
polyols with long, flexible chains between hydroxyl groups (such as 1,4-butanediol,
1,6-hexanediol, and diethylene glycol) may also be used to impart greater flexibility
in the resin.
326 PAINTS, VARNISHES, AND RELATED PRODUCTS
It should be pointed out that under high temperatures, such as those used for
alkyd resin synthesis, and in the presence of high acidity, etherification between
the hydroxyl groups of two polyol molecules may condense them into a new polyol
with a functionality of nþ n0 � 2, where n and n0 are the numbers of hydroxyl
groups of the two original molecules. The introduction of such high functionality
polyols plus the net reduction of total available hydroxyl groups can lead to an
increased danger of gelation during the poly-condensation process.
Monobasic Acids. The overwhelming majority of monobasic acids used in alkyd
resins are long-chain fatty acids of natural occurrence. They may be used in the
form of oil or free fatty acids. Free fatty acids are usually available and classified
by their origin, viz., soy fatty acids, linseed fatty acids, coconut fatty acids, etc. The
fatty acid composition of various types of fats and oils that are commonly used in
alkyd resins are given in Table 2.
The drying property of alkyd resins reflects directly that of the oil or fatty acids
in the resin structure, discussed earlier. It should be pointed out that alkyds based on
conjugated unsaturated fatty acids, such as those from tung and oiticica oils, dry so
fast that if not properly moderated, the surface layer will dry long before the under-
layer, resulting in a wrinkled surface due to the stresses created in the dried surface
layer. Therefore, in alkyd resins, tung oil and oiticica oil are primarily used to fur-
nish a minor portion of the fatty acids to improve drying properties. Even so, great-
er care must be exercised during the manufacturing process to avoid gelation, which
is caused by the dimerization of the fatty acid chains through a Diels-Alder addition
between the conjugated diene structure on one molecule and a double bond on
another molecule. It should be noted that nonconjugated diene groups, such as those
in linoleic and linolenic acids, may undergo isomerization to become conjugated.
Furthermore, ene-reaction could also occur between two unsaturated fatty acid
chains, which leads to gelation.
Rheineck and co-workers (44) have found that linolenic acid is responsible for
the high yellowing tendency of alkyds based on linseed oil fatty acids. Therefore,
alkyds intended for making white or light color enamels should avoid high linolenic
content fatty acids by choosing soy oil, safflower oil, or dehydrated castor oil
(DCO). Alkyds made with nondrying oils or their fatty acids have excellent color
and gloss stability. They are frequently the choice for white industrial baking enam-
els and lacquers.
Since the mid-1950s, tall oil fatty acids (TOFA) have become available in good
quality and large quantities. Refined grades of TOFA have degrees of unsaturation
rivaling that of soy acids. Since it is a year-round by-product from the paper indus-
try, its supply and price are more stable than agricultural products like soy fatty
acids. It is used extensively in medium- to long-oil alkyds, virtually as equivalent
to soy fatty acids. Although the minor quantities of rosin acids in TOFA may impart
some yellowing tendency, its lack of linolenic acid may be more than enough to
give as good or even better color retention than soy fatty acids. The typical proper-
ties of refined grades of commercial TOFA are given in Table 3.
A number of monobasic acids that are not derived from fats and oils have been
used in alkyd resins. However, except in the rare cases of making the so-called
ALKYD RESINS 327
TABLE 2. Fatty Acid Compositions of Fats and Oils Commonly Used in Alkyd Resins.
Fatty Acid Composition (Percent by Weight)
Oil Iodine Value Saponification Value Saturateda Palmitoleic Oleic Linoleic Linolenic Other
Castor 85.8 195 2.4 — 7.4 3.1 — Ricinoleic, 87.0; dihydroxystearic, 0.6
Castor, 125–135 191 2.4 — 8.0 86 3.0 About 33% of the linoleic is
dehydrated 9,11-conjugated.
Coconut 8.7 257 76.6 — 5.7 2.6 — Caprylic, 7.9; capric, 7.2; of the
saturated, lauric, 48.0 and
myristic, 17.5
Cottonseed 105.0 196 27.2 2.0 22.9 47.8 — Tetradecenoic, 0.1
Linseed 180 191 9.3 — 19.0 24.1 47.4 Lignoceric, 0.2
Menhaden 148–185 191 24.0 15.0 30.0 — — Highly unsaturated
C20H2(20� x)O2, 19; and
C22H2(22� x)O2, 12.b
Oiticica 192 11.3 — 6.2 — — Licanic, 82.5
Peanut 93.3 190 13.8 1.7 54.3 26.0 — Arachidic, 2.4; behenic 3.1:
lignoceric, 1.1
Rapeseed 102.3 175 6.1 1.5 12.3 15.8 8.7 Behenic, 0.7: lignoceric, 0.8;
eicosenole, 4.8; erucle, 47.8;
docosendienole, 1.5
Safflower 136.2 191 6.0 — 32.8 61.1 1
Soybean 132.6 193 13.4 1.0 23.5 51.2 8.5 Saturated C20-C24, 2.4
Sunflower 130.8 188 7.1 — 34.0 57.5 — Lignoceric, 0.4
Tung 192 5.0 — 5.0 3.0 — Eleostearic, 87
aAliphatic monocarboxylic acids, C12 to C20, principally palmitic and stearic.bx ¼ 4� 10.
Owing to incomplete halogen absorption, iodine values for conjugated acid oils by the usual methods (Wijs, Hanus, etc.) are both low and variable. The true value of fresh tung
oil, as determined by special method, is 248–252: that of oiticica oil is 205–220 (43).
oil-free alkyds for special purposes, they are used in conjunction with fatty acids to
modify resin properties. Rosin acids, primarily in the form of abietic acid, are the
most common type of such acids. They may be used in neat form or be brought in
as a part of TOFA. Presumably, the fused ring structure of rosin contributes to the
film hardness, initial gloss, and water resistance of the alkyd. However, color and
color retention, and exterior durability will be adversely affected if the rosin content
goes much above 5–6%. The drying rate of alkyds usually appears to be improved
with rosin modification. However, since rosin does not participate in the oxidative
drying mechanism that applies to polyunsaturated fatty acids, the true drying rate of
the alkyd resin would be reduced due to a reduction of the fatty acid unsaturation.
Synthetic saturated carboxylic acids (such as pelargonic acid, 2-ethylhexanoic acid,
and isoctanoic acid) and aromatic monobasic acids (such as benzoic acid and
p-alkyl-benzoic acids) can improve color retention, gloss retention, and exterior
durability even better than those based on castor or coconut fatty acids. The aro-
matic acids, similar to rosin, also give higher film hardness and faster apparent
drying rate.
5.5. The Concept of Functionality and Gelation
The concept of functionality and its relationship to polymer formation was first
advanced by Carothers (45) in 1929. Flory (46) greatly expanded the theoretical
consideration and mathematical treatment of polycondensation systems. Thus if a
dibasic acid and a diol are reacted to form a polyester, assuming there is no possi-
bility of other side reactions to complicate the issue, only linear polymer molecules
TABLE 3. Typical Properties of Refined Tall Oil Fatty Acidsa.
Grade Designation
Pamak Pamak Pamak Pamak Pamolyn Pamolyn
Characteristic 1 2 4A 4 200b 300a
Acid number 193 192 191 188 195 196
Iodine number 125 128 130 131 162 156
Total fatty acids, % 96.8 95.9 94.1 91.5 97 97
Saturated acids, % of free fatty acids 2.0 — — 4.0 <1 <1
Oleic 51.0 — — 51.0 22.0 21.0
Linoleic, nonconjugated 41.0 — — 39.0 68.0 39.0
Linoleic, conjugated 6.0 — — 6.0 10.0 40.0
Linolenic — — — — — —
Rosin acids, % 1.4 1.8 3.5 4.0 1.5 1.5
Unsaponifiables, % 1.8 2.3 2.4 4.5 1.5 1.5
Color, Gardner 3 3 4 6 3þ 3
Titer, �C 5 5 5 6 �28 �28
aData from Hercules, Inc. (Wilmington, Del.).bEnriched polyunsaturated fatty acids from highly refined TOFA.cSame as Pamolyn 200, with further treatment to isomerize the nonconjugated linoleic acid.
ALKYD RESINS 329
will be formed. When the reactants are present in stoichiometric amounts, the aver-
age degree of polymerization �xxn follows the equation:
�xxn ¼ 1=ð1� pÞ ð1Þ
where p is the extent of reaction, in fractions. Thus when the reaction is driven to
completion, theoretically, the molecular weight would approach infinity and the
whole mass would form one giant polymer molecule. Although the material should
theoretically be still soluble and fusible, it is considered and defined as a gel, and
this would be the only time that difunctional ‘‘monomers’’ could be polymerized to
gelation.
The functionality of the system f is the sum of all of the functional groups, i.e.,
equivalents, divided by the total number of moles of the reactants present in the
system. Thus in the above equimolar reaction system:
f ¼ ð1� 2þ 1� 2Þ=ð1þ 1Þ ¼ 2
However, when there are reactants with three or more functionalities participating
in the polymerization, branching and the formation of intermolecular linkages (i.e.,
cross-linking of the polymer chains) become definite possibilities. If extensive
cross-linking occurs in a polymer system to form network structures, the mobility
of the polymer chains is greatly restricted. Then the system would lose its fluidity
and transform from a moderately viscous liquid to a gelled material with infinite
viscosity. The experimental results of several such reaction systems reported by dif-
ferent investigators are collected in Table 4.
The data in Table 4 show that when the reactants are present in stoichiometric
proportions, gelation occurs before the completion of esterification, and the extent
of reaction p reached at the gel point depends on the functionality of the system.
Carothers (47) showed that at the gel point, p ¼ 2=f . Thus, to avoid premature
gelation, the polymerization system should have an average functionality of no
more than 2. This can be accomplished by adding low functionality reactants
and/or adding an excess amount of one of the reactants, usually the one with high
functionality constituents. The latter has the net effect of reducing the functionality
of the reactant. For example, if a 20% excess of glycerol over the stoichiometric
TABLE 4. Gel Points of Polyesterification Reaction Systems with Stoichiometric
Reactants (46).
Percent Esterification
Polybasic Acid (COOH) Polyol (OH) f at Gel Point
Adipic (0.707)þ tricarballylic (0.293) di-EG (1.0)a 2.103 0.911
Dibasic (1.0) glycerol (1.0) 2.400 0.765
Adipic (1.0) PE (1.0)b 2.667 0.578
aDiethylene glycol.bPentaerythritol.
330 PAINTS, VARNISHES, AND RELATED PRODUCTS
amount required to esterify all of the carboxyl groups present in the formula is
added, the glycerol would have an effective functionality of 3/1.2, or 2.5. Fre-
quently, both of these measures are taken to safeguard against premature gelation.
Patton (48) showed that for alkyd resins, the extent of the reaction at gel point was
pc ¼ 2=f ¼ 2mo=eo
where eo is the total effective equivalents of all of the reactants present at the begin-
ning of the reaction (i.e., the excess reactants are discounted in the manner dis-
cussed above), mo is the total number of moles of all reactants at the beginning,
and f is the effective average functionality of the formulation.
5.6. Microgel Formation and Molecular Weight Distribution
Bobalek and co-workers (49) observed that the behavior of alkyd resin reaction
often deviates from that predicted by the theory of Flory. They proposed a mecha-
nism of microgel formation by some of the alkyd molecules at a relatively early
stage of the reaction. The microgel particles would be dispersed and stabilized
by smaller molecules in the remaining reaction mixture. As polyesterification pro-
ceeds, more microgel particles would be formed, until finally a point is reached at
which they could no longer be kept separated. The microgel particles would then
coalesce or flocculate, phase inversion would occur, and the entire reaction mass
would be ‘‘gelled.’’ They showed that the drying capability of an alkyd resin comes
primarily from the microgel fraction and, ‘‘when the highest molecular weight frac-
tion representing about 20% of the total was removed through fractionation, the
residual linoleic alkyd lost all ability to air dry to a hard film.’’
Solomon and co-workers (50, 51) further elaborated on the microgel theory by
proposing the formation of micelles as precursors of microgels. They proposed that
when some of the molecules have grown to reach certain fatty acid: polyester ratios,
surface activity develops to form micelles. The polyesterification reactivity at the
surface of the micelles would be preferentially greater, which would lead to the
eventual formation of microgels. From electronmicroscopy evidence, they observed
that the size of microgels increased with reaction time, and particle diameters as large
as 2m have been reported. Functional groups such as OH groups in the microgel
particles are believed to be buried in the structure and not available for reactions.
Whereas in polyesterification reactions without fatty acids, at all stages of the reac-
tion up until the physical gelation of the reaction mixture, the hydroxyl values cor-
responded with the calculated values. Furthermore, the oil-free systems showed no
sign of microgel formation under electron microscope, and the reaction mixture
would undergo a sudden change from a soluble polymer to a gelled mass. The reac-
tion temperature for alkyd preparation in both of the above references was kept at
no more than 200�C, well short of what would normally be required for the bodying
of unsaturated oils in the absence of an oxidizing reagent. This indicates that poly-
merization between unsaturated fatty acids of the resin molecules is not necessary
for the formation of microgels.
ALKYD RESINS 331
Kumanotani and co-workers (52–55) further confirmed the formation of micro-
gels by characterizing fractions of alkyd resins from preparative GPC columns.
Their results showed that the presence of microgel can be detected even in low
molecular weight fractions. Colloidal gel particles up to 10þ mm in diameter
were observed in the high molecular weight (>105) fractions, with or without unsa-
turated fatty acids in the alkyd formulation. However, the unsaturated fatty acids
made a significant contribution to the formation of the colloidal particles. Higher
reaction temperature led to higher molecular weight and broader molecular weight
distribution. Acid value and hydroxyl value each went through a minimum in the
middle fractions (molecular weight about 103–104), whereas the polyester: mono-
acid ratio increased with the molecular weight of the fraction. Cured films from
alkyds with greater amount of colloidal fractions gave better thermomechanical
properties. Finally, the high molecular weight colloidal fractions were preferentially
adsorbed by pigment particles and would thus stabilize the pigment dispersion in
the coating formulation.
5.7. Basic Principles for the Designing of Alkyd Resins
The process of alkyd resin designing should begin with the following question:
what would be the intended application(s) of the resin? The application would
dictate property requirements, such as solubility, viscosity, drying characteristics,
compatibility, film hardness, film flexibility, acid value, water resistance, chemical
resistance, environmental endurance, etc. With these targets in mind, a selection on
oil length, and a preliminary list of alternative choices of ingredients can then be
made. For commercial production, the raw material list is screened based on consi-
derations in material cost, availability, yield, impact on processing cost, and poten-
tial hazard to health, safety, and the environment. The list may be further narrowed
by limitations imposed by the production equipment or other considerations. Once
the oil length and ingredients are chosen, the first draft of a detail formulation for the
resin can then be made.
It would be highly desirable that one could rely on a simple equation or formula
to obtain the optimum formulation of the alkyd resin with the chosen ingredients,
and several approaches have been proposed for such purpose (56–59). However, the
complexity of the alkyd reaction system has rendered these equations to be of no
more value than providing a first approximation of a starting formula. The causes of
the complexities include the formation of intramolecular cyclic structures, which
would reduce the chance of gelation; the etherification of polyols, which would
increase the chance of gelation by forming higher functionality materials and redu-
cing the number of hydroxyl groups available for esterification; the cross-linking
between unsaturation groups, especially the conjugated double bonds, which would
increase the chance of gelation; and the phenomenon of microgel formation.
Except when nondrying alkyds are used strictly as plasticizers for other thermo-
plastic polymers, alkyd resins do not remain as a thermoplastic material in their
ultimate application. The film integrity is largely derived after the resin molecules
have been cross-linked, either through the unsaturation functionalities on their fatty
332 PAINTS, VARNISHES, AND RELATED PRODUCTS
acid side chains or through the reactions of their residual hydroxyl or carboxyl
functionalities with such cross-linking agents as amino resins or polyisocyanate
materials. In a sense, alkyds are usually made and applied as B-stage resins. There-
fore, it is not necessary to build the molecules of alkyd resins to huge molecular
weights, as one would for thermoplastic polymers. In fact, too high a molecular
weight would lead to poor solubility and high solution viscosity and would be un-
desirable for practical applications. Most of the published data show that the aver-
age molecular weight of alkyds is less than 10,000. Nevertheless, within the
practical limits, it is still preferred to have a linear backbone structure and high
molecular weight to give the best film-forming and film properties. Alkyd formula-
tions with an equimolar ratio of dibasic acids: polyols tend to have the best chance
of achieving a linear molecular structure and high molecular weight.
Thus a simple molecular approach is favored by some of the alkyd chemists for
deriving the starting formulation. The basic premise of this approach is that when
the total number of moles of polyols is equal to or slightly larger than that of the
dibasic acids and the hydroxyl groups are present in an empirically prescribed
excess amount, the probability for gelation to occur would be small. Table 5 lists
the empirical requirements of excess hydroxyl groups based on the oil (fatty acid)
length of the alkyd. The values were developed based on experimental experience
(57, 58). With the new understanding that some of the hydroxyl groups would be
buried in microgel structures (49–55), such requirements may be better rationa-
lized. The procedure of this method for formulating alkyd resins will be illustrated
with examples.
The first example demonstrates the formulations of a 50% soy oil alkyd for
baking enamels. The preliminary selection of ingredients would be alkaline refined
soy oil, phthalic anhydride (PA), and pentaerythritol. The basis for calculation is
1 mole of PA. From Table 5, the excess OH recommended at 50% oil length
is 25%. Therefore, the quantity of PE required, in equivalents, would be
EPE ¼ 1� 2� ð1þ 0:25Þ ¼ 2:5 eq: ¼ 0:625 moles
TABLE 5. Excess Hydroxyl Content Required in Alkyd Formulations.
Oil Length, Percent Percent Excess OH Based Percent Excess OH
Fatty Acida on Diacid Equivalents in Finished Resin
62 or more 0 0
59–62 5 0–5
57–59 10 5–10
53–57 18 10–15
48–53 25 15–20
38–48 30 20–25
29–38 32 25–30
aBased on C18 fatty acids with average equivalent weight of 280. If the average
equivalent weight of the monobasic acids is significantly different, adjust
accordingly.
ALKYD RESINS 333
Since the total polyol is to be equimolar to PA, the glycerol from the soy oil will,
therefore, be ð1� 0:625Þ ¼ 0:375 moles, which gives ð3� 0:375Þ ¼ 1:125 moles
of soy fatty acids. The ingredients can be listed as follows:
The above formulation does not meet the test of 50% oil length. The oil content
must reduced. A reduction in oil would cause a corresponding reduction in glycerol,
consequently, free glycerol is added to make up the loss. Let MPE ¼ X, MGly ¼ Y ,
and Moil ¼ Z. Since the total polyols is to be equimolar to dibasic acids, X þ YþZ ¼ 1. The 25% excess OH requirement defines 4X þ 3Y ¼ ð2� 1:25Þ ¼ 2:5, and
the 50% oil length requirement gives the following:
880Z=ð148þ 141:6X þ 93Y þ 880Z � 18Þ ¼ 0:5
where 880, 148, 141.6, 93, and 18 are the molecular weights of the oil, PA, PE,
glycerol, and water, respectively. When solve the simultaneous equations to find
X ¼ 0:221, Y ¼ 0:539, and Z ¼ 0:240. Thus the ‘‘final’’ formulation is listed as
follows:
The above formulation meets all of the requirements of the resin design, i.e., equi-
molar PA and polyols, 25% excess OH, and 50% oil.
The next example shows the formulation of a 50% TOFA alkyd for baking
enamels. Assume that PA, PE, ethylene glycol (EG), and refined TOFA with
4% rosin acids are the chosen ingredients. From the given constraints, the
Ingredient M COOH OH Weight (g)
PA 1.0 2.000 — 148.0
Soy oil 0.240 0.720 0.720 211.2
Glycerol 0.539 — 1.617 50.1
Tech-PE 0.221 — 0.884 31.3
Total 2.000 2.720 3.221 440.6
Water 1.0 — — (18.0)
Resin — — — 422.6
Ingredient M COOH OH Weight (g)
PA 1.0 2.000 148.0
Soy oil 0.375 1.125 1.125 330.0
Tech-PE 0.625 — 2.500 88.5
Total 2.000 3.125 3.625 566.6
Water 1.0 — — (18.0)
Resin — — — 548.5
334 PAINTS, VARNISHES, AND RELATED PRODUCTS
following simultaneous equations can be established. Let MEG ¼ X, MPE ¼ Y , and
MTOFA ¼ Z.
X þ Y ¼ 1
2X þ 4Y ¼ 2� ð1þ 0:25Þ þ Z
295Z � ½148þ 141:8Y þ 62X þ 295Z � 18� ð1þ ZÞ� ¼ 0:5
Solve the equations, to find X ¼ 0:362, Y ¼ 0:638, and Z ¼ 0:776. Therefore, the
‘‘final’’ formulation can be listed as follows:
The percent excess OH ¼ ð3:276� 2:776Þ=2 ¼ 25%, and the oil length ¼228:9=457:6 ¼ 50% TOFA.
The ‘‘final’’ formulations derived in the above examples are meant to be only the
starting formulations. They should be fine-tuned based on small-scale laboratory
experiments before being used in plant production.
Since the molecular chain length or the degree of polymerization is a function of
the extent of the reaction as shown in equation 1, the alkyd reaction is usually car-
ried to a point short of completion, i.e., to a finite acid number to guard against
premature gelation. It has been shown that the esterification of phthalic anhydride
was slower and showed higher temperature dependence, i.e., higher activation
energy, than that of fatty acids (60–62). Therefore, one may assume that the residual
acidity belongs to unreacted dibasic acids, which contributes to the limiting of
chain growth. In real practice, an additional safety margin against premature
gelation is provided by having a slight molar excess of polyols over dibasic acids
in the alkyd formulation. If the molar ratio between the polyols and the dibasic
acids is r, equation (1) may be rewritten as:
�xxn ¼ ð1þ 1=rÞ=½ð2=rÞð1� pÞ þ 1� 1=r� ð2Þ
which indicates that a fractional increment in r and/or a fractional reduction in p
would give a substantial reduction in �xxn. Generally, the value of r is chosen between
1 and 1.05.
Ingredient M COOH OH Weight (g)
PA 1.000 2.000 — 148.0
Tech-PE 0.638 — 2.552 90.3
EG 0.362 — 0.724 22.4
TOFA-4 0.776 0.776 — 228.9
Total 2.776 2.776 3.276 489.6
Water 1.776 — — (32.0)
Resin — — — 457.6
ALKYD RESINS 335
5.8. Chemical Procedures for Alkyd Resin Synthesis
Different chemical procedures may be used for the synthesis of alkyd resins. The
choice is usually dictated by the choice of the starting ingredients.
Alcoholysis Process. Cost and availability often dictate that oil, rather than free
fatty acids, be used as raw material for alkyd synthesis. Since oil, in the form of
triglycerides, is essentially inert and would not participate in the polyesterification
reaction, heating the oil with the polyol and the dibasic acid would result in the
formation of seedy polycondensates between the polyol and the polybasic acids
leaving the oil unreacted. The two phases thus would be incompatible with each
other. Therefore, the triglycerides must first react with additional polyol to redistri-
bute the fatty acids among all of the polyols, thereby liberating free hydroxyl groups
from the oil for further reaction with the dibasic acids. The reaction is alcoholysis.
It is usually catalyzed by basic compounds such as metal oxides, hydroxides, salts,
or soaps such as naphthanates. In the past, litharge was the most popular choice as
the catalyst. It was found that on a molar basis lead compounds were the most effi-
cient among the 36 that were included in the study (58). In recent years, due to the
concern of lead poisoning from the resultant coatings, lithium hydroxide, sodium
hydroxide, or calcium oxide have been commonly used. The dosage of these cata-
lysts usually ranges from 0.01 to 0.06% metal based on the weight of the oil for lead
and 0.008 to 0.02% for lithium or calcium. The amount of catalyst added should be
kept at the minimum required for completing the reaction in an acceptable batch
time. They may cause poor color, poor water resistance, or haziness in the final
resin.
Ideally, 2 moles of polyol would react with 1 mole of triglyceride to form 3 moles
of monoester. In reality, the reaction would reach an equilibrium, whereby some
amount of diesters and triesters and neat polyol, including glycerol and the added
polyol, would coexist in the reaction mixture. The composition of the alcoholysis
product at equilibrium from soy oil and glycerol (1 : 2 mole ratio), and soy oil and
monopentaerythritol have been reported as follows (63):
Mole Percent
—————————————
Component Oil-Glycerol Oil-Mono-PE
Glycerol
Monoester 42 20.6
Diester 21 6.2
Triester 3 2.0
Free glycerol 33 14.0
PE
Monoester 29.0
Diester 16.8
Triester 5.1
Tetraester Negligible
Free PE 6.3
336 PAINTS, VARNISHES, AND RELATED PRODUCTS
Diols, such as ethylene glycol, are usually not added during the alcoholysis step.
This is because their monoesters have only one remaining hydroxyl group and
would function as chain stoppers, thus severely limiting their utility in the structure
design of the resin molecules.
In general practice, the oil is first heated to 230–250�C under an inert gas blanket
and agitation. The catalyst, usually predispersed in a small quantity of the oil, and
the polyol, usually at 2 times the molar quantity of the oil present in the reactor, are
added. The batch is reheated to and maintained at the desired temperature, usually
in the 230–250�C range. The progress of the reaction is monitored by periodical
sampling from the reactor and checking miscibility with anhydrous methanol.
This is because triglycerides are not soluble in methanol, whereas monoglyceride
is. When a volume of the alcoholysate can tolerate three or more volumes of metha-
nol without becoming turbid, the alcoholysis process is considered complete.
Acidic contaminants are poisonous to the alcoholysis catalysts and must be
avoided. If the oil has a high acid number, or there are high acidity residues left
in the reactor from the previous batch, such as sublimed phthalic anhydride con-
densed under the dome of the reactor, the reaction can be severely retarded. A
longer batch time or additional amount of the catalyst would then be required.
Both are undesirable.
When the alcoholysis step is complete, the polybasic acid(s) and the balance of
polyol, if any, are added. The batch is reheated to and maintained at about 250�C to
carry out the polycondensation step to the desired endpoint, usually a combination
of the acid value and viscosity of the resin.
Fatty Acid Process. When free fatty acids are used instead of oil as the starting
component, the alcoholysis step is avoided. All of the ingredients can, therefore,
be charged into the reactor to start a batch. The reactants are heated together,
under agitation and inert blanket, until the desired end point is reached. Chen
and Kumanotani (64) reported that alkyds prepared by the fatty acid process
have narrower molecular weight distribution and give films with better dynamic-
mechanical properties.
A modified form of the fatty acid process, dubbed ‘‘high polymer alkyd tech-
nique’’ was reported (65). A portion of the fatty acids is withheld in the first stage
of the process to allow the polycondensation between the dibasic acid and the
polyol to have a better chance of extending the polyester chain without being termi-
nated by the monoacids. After the acid value of the reactant has reached a desired
low level, indicating the completion of the poly-condensation, the remaining
portion of fatty acids is then added to complete the process. The resins prepared
by this technique have more linear backbone chain structure, higher molecular
weight, and higher viscosity than the corresponding ones with identical formulation
but prepared by the conventional process.
Fatty Acid–Oil Process. When oil represents only a minor portion (33% or less)
of the total furnish of fatty acids in an alkyd formulation, the alcoholysis step may
be avoided. All of the ingredients, dibasic acid, polyol, oil, and free fatty acids may
be charged together into the reactor and proceed as in the fatty acid process. Appar-
ently, the oil is incorporated into the resin by ester interchange at the reaction
ALKYD RESINS 337
temperature. The resultant resins give higher viscosity (4), faster surface drying,
and slower through-dry (3). If the oil content is too high, not enough of it may
be incorporated in time, then it, would result in a partial gelation to form ‘‘seeds.’’
Acidolysis Process. As mentioned previously, isophthalic and terephthalic acids
are difficult to process in ordinary alkyd preparation methods, due to their high
melting point and low solubility in the reaction mixture. An acidolysis process
was developed for this purpose (6). The dibasic acid is heated together with the
oil in the resin formulation under agitation and inert gas blanket to about 280�C,
holding for about 40 min. In this reaction, which is self-catalyzed by the acidity
of the reaction mixture, an ester interchange occurs. A carboxyl group of the dibasic
acid displaces that of a fatty acid on the oil molecule and splits off the fatty acid.
The completeness of the acidolysis reaction is determined by a tedious extraction
of the oil phase and analysis of its free fatty acid content by titration. The analysis
takes several hours to complete. Rapid test methods, comparable to the methanol
miscibility test for alcoholysis, that could be used for process control of the acido-
lysis reaction have yet to be developed. Therefore, the process is normally con-
trolled by reaction time and temperature, based on experience. After acidolysis,
the reactant temperature is dropped to about 230�, the polyol is charged and heated
back up to the desired temperature to bring the esterification step to the desired
end point. The acidolysis process is not suitable for phthalic anhydride or other
dibasic acids with a high tendency to sublime.
Alkyd Resin Production Processes. Parallel to the above chemical procedures,
the processing method may also be varied with different mechanical arrangements
to remove by-product water, to drive the esterification reaction toward completion.
Fusion Process. In the fusion process, also frequently referred to as fusion cook,
inert gas is continuously sparged from the bottom of the reactor to carry away water
vapor from the reaction mixture. The exhaust is then either vented away or sent to a
fume scrubber, which is frequently a small vessel with water atomizing nozzles.
After the reaction is completed, the finished resin may be discharged, filtered,
and packaged without solvent. More frequently, it is cooled to a safe temperature,
then dissolved with the desired type and amount of solvent in a thinning tank, fil-
tered, and packaged, or pumped to a storage tank. The reactor usually needs to be
cleaned by charging a small volume of solvent into the vessel and heated to reflux
for an appropriate time period. If deemed necessary, the vessel is further cleaned
by digesting with caustic soda solution.
The fusion process has the advantage of simplicity in mechanical arrangement.
However, it has several significant disadvantages. Low boiling and/or subliming
ingredients, such as glycols and phthalic anhydride, would be lost during the reac-
tion causing the product composition and its properties to deviate from the design.
The material loss causes an increase in the cost of the resin. Reactants as well as the
product may adhere to the reactor walls above the surface level of the charge, which
will contaminate or even become catalyst poisons to the subsequent batches. And
the resin produced from a fusion cook is more prone to develop dark colors. For
these reasons, most of the manufacturers have discontinued the practice of fusion
cook, unless it is dictated by the existing equipment.
338 PAINTS, VARNISHES, AND RELATED PRODUCTS
Solvent Process. In the solvent process, or solvent cook, the water formed from
the reaction is removed from the reactor as an azeotropic mixture with an added
solvent, typically xylene. Usually between 3 to 10 weight percent, based on the
total charge of the solvent, are added at the beginning of the esterification step.
The mixed vapor passes through a condenser. The condensed water and solvent
have low solubility in each other, and phase separation is allowed to occur in an
automatic decanter. The water is removed, usually to a measuring vessel. The
amount of water collected can be monitored as one of the indicators of the extent
of the reaction. The solvent is continuously returned to the reactor to be recycled. A
typical equipment for this process is shown in Figure 2. The reactor temperature is
Figure 2. Equipment for solvent processing of alkyd resins. Courtesy of Hercules Inc.
(Wilminton, Del.).
ALKYD RESINS 339
modulated by the amount and type of refluxing solvent. Typical conditions are as
follows.
The solvent vapor also serves as a blanket in the reactor. The processing solvent is
usually left in the product as part of the dilution solvent.
The refluxing solvent provides a constant wash to the reactor, and brings back
the reactants that had escaped out of the reaction mixture. The reaction temperature
is better controlled by the constant refluxing, and the viscosity of the reaction mix-
ture is lower, which improves the effectiveness of the agitation. The product usually
has better color and is more uniform than those made by the fusion process. Ordi-
narily, the reactor requires no more than a solvent wash to be clean enough for the
next batch. These advantages far outweigh the higher cost of the production facility.
Therefore, few would consider building a new alkyd plant without solvent process
capability.
When low boiling ingredients such as ethylene glycol are used, a special provi-
sion in the form of a partial condenser will be needed to return them back into the
reactor. Otherwise, not only would the balance of the reactants be upset and the raw
material cost of the resin be increased, they would also become part of the pollutant
in the waste water and incur additional water treatment costs. Usually, a vertical
reflux condenser or a packed column is used as the partial condenser, which is
installed between the reactor and the overhead total condenser (Figure 3). The
temperature in the partial condenser is monitored and maintained at a level to effect
a fractionation between water, which is to pass through the reactor, and the glycol
or other materials, which is to be condensed and returned to the reactor. If the frac-
tionation is poor and water vapor is also condensed and returned, the reaction will
be retarded and result in a loss of productivity. As the reaction proceeds toward
completion, water evolution slows down, and most of the glycol will have been
combined into the resin structure. The temperature in the partial condenser may
then be raised to facilitate the removal of water vapor.
5.9. Process Control
The progress of the alkyd reaction is usually monitored by periodical determina-
tions of the acid number and the viscosity (solution in a suitable solvent and at
an appropriate concentration) of samples taken from the reactor. The frequency
of sampling is commonly every half hour. The general practice is to plot the deter-
mined values separately against time on semilogarithmic coordinants (Figure 4).
Solvent Weight Percent Temperature (�C)
Xylene 3 251–260
Xylene 4 246–251
Xylene 7 204–210
High flash naphtha 10 204–210
340 PAINTS, VARNISHES, AND RELATED PRODUCTS
Toward the end of the reaction, the resin viscosity tends to increase exponentially.
Gelation in the reactor is always a threat, due either to what the formulation would
theoretically allow by the completion of the polyesterification or to the occurrence
of some of the side reactions. After the onset of gelation, it would progress extre-
mely rapidly and would be almost impossible to arrest. Therefore, it is routine to
Figure 3. Solvent-processing equipment using a partial condenser. Courtesy of Hercules Inc.
(Wilmington, Del.).
ALKYD RESINS 341
extrapolate the plots in Figure 4 when predicting the point at which to terminate the
reaction in time to prevent gelation. If gelation should occur in the reactor, it would
cause not only the loss of product but also significant down time for cleaning the
reactor. Some alkyd practitioners have found that a rapid addition of a large quan-
tity of raw oil quenches the runaway gelation, disperses the gel, and significantly
eases the cleanup operation. A technique of injecting water or steam during the
condensation process to reverse or retard gelation has been reported in the patent
literature (66).
Figure 4. Alkyd reaction control plots.
342 PAINTS, VARNISHES, AND RELATED PRODUCTS
6. SAFETY AND ENVIRONMENTAL PRECAUTIONS
The manufacturing of alkyd resins involves a wide variety of organic ingredients.
While most of them are relatively mild with low toxicity, some of them such as
phthalic anhydride, maleic anhydride, solvents, and many of the vinyl (especially
acrylic) monomers are known irritants, or skin sensitizers, and are poisonous to
humans. Persons involved should be thoroughly familiar with the hazard potential
of each and every one of the chemicals by consulting the material safety data sheets
provided by the suppliers and practicing the recommended safety precautions in
handling the materials. The use of personal safety equipment such as protective
goggles, gloves, clothing, and respiratory devices should be diligently observed.
Since large quantities of highly flammable solvents are routinely handled in an
alkyd plant, fire safety should be the utmost in everyone’s mind. Electrical equip-
ment and power circuitry in the plant should conform to all applicable codes, and
all equipment should be properly grounded. The areas for the reactors and storage
tanks should be separated by fire walls and must be adequately ventilated. The
storage tanks should be blanketed by inert gas. A slight positive pressure of inert
gas should be maintained in the reactor or storage tanks during discharge of the
resin or resin solution to prevent air from being sucked into the vessel to form
an explosive mixture with the solvent vapor.
With the ever increasing awareness of the need for environmental protection,
the emission of solvent vapors and organic fumes into the atmosphere should be
prevented by passing the exhaust through a proper scrubber. The solvent used for
cleaning the reactor is usually consumed as part of the thinning solvent. Aqueous
effluent should be properly treated before discharge.
7. MODIFICATION OF ALKYD RESINS BY BLENDINGWITH OTHER POLYMERS
As mentioned earlier, one of the important attributes of alkyds is their good com-
patibility with a wide variety of other coating polymers. This good compatibility
comes from the relatively low molecular weight of the alkyds and the fact that the
resin structure contains, on the one hand, a relatively polar and aromatic backbone
and, on the other hand, many aliphatic side chains with low polarity. The alkyd
resin involved in a blend with another coating polymer may serve as a modifier
for the other film former, or it may be the major film former and the other polymer
may serve as the modifier for the alkyd to enhance certain properties. The following
describes some of these compatible blends.
Nitrocellulose-based lacquers often contain a fair amount of short- or medium-
oil alkyds to improve flexibility and adhesion. The most commonly used are
short-oil nondrying alkyds. Amino resins or urethane resins with residual isocya-
nate functional groups may be added to cross-link the coating film for improved
MODIFICATION OF ALKYD RESINS BY BLENDING WITH OTHER POLYMERS 343
solvent and chemical resistance. The major applications are furniture coatings, top
lacquer for printed paper, and automotive refinishing primers.
Amino resins are probably the most important modifiers for alkyd resins. Butyl-
ated urea- or melamine–formaldehyde resins are compatible with alkyds. They
react with the free hydroxyl groups of the alkyd to effect cross-linking and to impart
hardness, mar resistance, chemical resistance, and durability to the coating. Short-
or medium-oil alkyds of both drying and nondrying types are frequently used. Color
and color retention requirements often dominate the choice of the alkyd. Many
industrial baking enamels, such as those for appliances, coil coatings, and auto-
motive finishes (especially refinishing enamels), are based on alkyd-amino resin
blends. Some of the so-called catalyzed lacquers for finishing wood substrate
require low bake or no bake at all.
Chlorinated rubber is often used in combination with medium-oil drying type
alkyds. The alkyd gives better toughness, flexibility, adhesion, and durability, and
the chlorinated rubber contributes to faster dry and better resistance to water
and chemicals. The major applications are highway traffic paint, concrete floor,
and swimming pool paints.
Vinyl resins of the type that are the copolymers of vinyl chloride and vinyl acet-
ate and that contain a fair amount of hydroxyl groups (from the partial hydrolysis of
vinyl acetate) and/or carboxyl groups (e.g., from copolymerized maleic anhydride)
may be formulated with alkyd resins to improve application properties and adhe-
sion. The blends are primarily used in making marine topcoat paints.
Synthetic latex house paints sometimes contain emulsified long-oil or very long
oil drying alkyds to improve adhesion to chalky painted surfaces.
Silicone resins with high phenyl contents may be used with medium- or short-oil
alkyds as blends in air-dried or baked coatings to improve heat and weather resis-
tance, whereas the alkyd component contributes to adhesion and flexibility. Major
applications include insulation varnishes, heat-resistant paints, and marine coatings.
7.1. Chemically Modified Alkyd Resins
While blending with other coating resins provides a variety of ways to improve the
performance of alkyds, or vice versa, chemically combining the desired modifier
into the alkyd structure would eliminate the compatibility problem and give a more
uniform product. Several such chemical modifications of the alkyd resins have
gained commercial importance, and are described below.
Vinylated alkyds are alkyd resins that have been incorporated with a significant
amount (20–60% by weight) of vinyl monomers (such as styrene, vinyl toluene, and
methyl methacrylate) by grafting the monomers through a free-radical mechanism
onto unsaturated reaction sites in the resin molecules. The modified resin embodies
the good attributes of ease of application, good wetting, and adhesion from the
alkyd as well as fast solvent release, hardness, and weather resistance from the vinyl
modification. The common objective of such a modification is for achieving a
drying rate comparable to that of lacquer materials. The reaction sites on alkyd
resin molecules are primarily the allylic carbons on unsaturated fatty acid chains
344 PAINTS, VARNISHES, AND RELATED PRODUCTS
and the double bond of a,b-unsaturated dibasic acids. Free radicals, generated from
the thermolysis of such free-radical initiators as benzoyl peroxide, dicumyl perox-
ide, and di-t-butyl peroxide are usually required to kick off the reaction. Ideally, the
initiating species would attack the active sites on the resin molecules and all of the
added monomers would be evenly distributed in grafted side chains. In reality, it is
inevitable that part of the monomers would engage in homopolymerization, and
some of the resin molecules would remain unmodified. The presence of a large
amount and high molecular weight homopolymer of the vinyl monomer would
lead to incompatibility and result in a hazy product. Methods that have been
used to minimize homopolymerization include using fatty acids having conjugated
diene structure, using maleic anhydride as part of the dibasic acids for the alkyd,
choosing initiators such as peroxides or hydroperoxides that tend more to extract
allylic protons than to add to double bonds, avoiding initiators that would decom-
pose at very low temperatures, adding the monomer gradually along with an appro-
priate amount of the initiator, choosing monomers that would have a more
favorable tendency to copolymerize with the active species on the alkyd resin,
and properly maintaining the reaction temperature. Chain transferring is the pre-
ferred mechanism for terminating chain growth from the addition polymerization
of the monomer. Usually, the solvent, the fatty acid chain, and the monomer are
effective chain-transfer agents. If an additional transferring agent is used, care
must be exercised, or too much of it could cause the formation of a large amount
of very low molecular weight homopolymers, and would result in poor film proper-
ties. Occasionally, vinylation is first performed on the fatty acids or the oil before
the alkyd reactions.
It should be emphasized that the presence of a large amount of either conjugated
fatty acids or maleic anhydride in the alkyd formulation gives rise to a high degree
of probability of premature gelation during the alkyd reaction. An allowance must
be made in the alkyd formulation, and the polyesterification is frequently termi-
nated at a relatively high acid number (about 15), to avoid gelation. It has been
reported that the optimum amount of maleic anhydride in the alkyd is an amount
having a maleic group in one-third of the resin molecules (17).
A common procedure for the preparation of vinylated alkyds is as follows: first,
a base alkyd resin is brought to the desired end point. The resin is then cooled to
about 160�C and often diluted with aromatic thinner. Next, the desired monomer is
added, usually at about 20–60% based on the final product, followed by an appro-
priate amount of a free-radical initiator. Alternatively, a premix of the monomer and
the initiator is added at a controlled rate over most of the reaction. Then the reaction
is brought to monomer reflux, until the residual monomer content has dropped
below a specified level. The residual monomer, if any, is stripped away before the
product is diluted in a solvent, filtered, and packaged.
Silicone alkyds are etherification products of alkoxy-polysiloxane oligomers
and the free hydroxyl groups of alkyd resins (67, 68). The property improvements
and applications are similar to those of the alkyd-silicone blends, with the added
advantage of incorporating the stable ��Si��O��C�� structure into the alkyd mole-
cules. The preferred silicone oligomers are those with high phenyl contents, and
MODIFICATION OF ALKYD RESINS BY BLENDING WITH OTHER POLYMERS 345
the alkyds at long- or medium-oil length based on polyols with primary hydroxyls.
To improve the thermal stability effect imparted by the silicone modification
further, one can use isophthalic alkyds rather than the phthalic type. The etherifica-
tion reaction may be carried out on an alkyd resin designed for the purpose or on the
polyol before it is used in alkyd preparation. The silicone content of the modified
alkyd lies usually between 20 and 60% of the total product.
Urethane alkyds, or uralkyds, are alkyds with a part or even all of the dibasic
acids replaced by diisocyanates. The isocyanate group, ��N����C����O, reacts with
the hydroxyl group of a polyol, at low temperature, to form a urethane linkage,
��NHC(O)O��, without spitting out water as a by-product. Toluene diisocyanate
(TDI) is commonly used for such modification. It is commercially supplied as an
80 : 20 mixture of 2,4- and 2,6-isomers. The ��NCO� group para to the methyl
group has about 8 times greater reactivity than the one on the ortho position, which
aids greatly the control of the reaction. Since the NCO group is reactive with labile
protons, water must be excluded from the reaction system. The esterification reac-
tion of the base alkyd must be brought to the desired end point with the by-product
water removed, and the temperature lowered to about 100�C to prevent any conti-
nuation of the esterification before the introduction of the NCO reactant. TDI is
highly toxic and is usually handled in a closed system under a dry inert gas blanket.
Metallic soaps, such as dibutyltin dilaurate, stannous octoate, and calcium naphtha-
nate, are used as reaction catalysts. The reaction is vigorous and exothermic. There-
fore, the reaction temperature is maintained under 135�C, and great care must be
exercised to bring the reaction under proper control.
Uralkyds have superior adhesion, hardness, abrasion resistance, durability, and
chemical resistance to the unmodified alkyds. They find major applications in wood
floor finishes, marine coatings, metal primers, and maintenance paints.
Phenolic resins are well known for their contribution in improving hardness,
gloss, and water and chemical resistance in oleoresinous varnishes. Those based
on p-alkyl-substituted phenols and with heat-reactive methylol groups have also
been incorporated into alkyd resins. The reaction has not been well studied. Pre-
sumably, the methylol group would react with the unsaturation functionality on
the fatty acid chain to form the chroman structure, similar to what is believed to
have occurred in the varnish. Etherification between the methylol group and free
hydroxyl of the alkyd resin, catalyzed by the residual acidity in the resin, would
be another possible reaction.
Polyamide modified alkyds show a special rheological behavior—they are thix-
otropic (69, 70). Typically, the polyamide resin would be of the type based on dimer
acids, i.e., dimerized unsaturated fatty acids, and aliphatic diamines, such as ethy-
lene diamine. These would react to form polyamide resins with low acid and amine
values. The alkyd resin would be a medium- or long-oil drying alkyd. The reaction
products from the polyamide and the alkyd are gel-like materials that undergo a
time-dependent shear thinning and recover to the gel-like state after the shearing
action is stopped. This allows the preparation of ‘‘no-drip’’ paints, which are
easy to brush and can be applied at high film thickness from a single coat with little
or no danger of sagging. Pigment settling during storage of the paint is also
346 PAINTS, VARNISHES, AND RELATED PRODUCTS
minimized. The major applications are flat oil-based architectural paints and main-
tenance paints. Generally, up to 10% of the polyamide based on the weight of the
alkyd is added to the alkyd and heated at normal alkyd reaction temperature under
agitation. Ester interchange reaction takes place, and fragments of the polyamide
resin become chemically bonded to the alkyd. The modified alkyd serves as a com-
patibilizer for the mutually insoluble unreacted polyamide and alkyd to form a
gellike structure. The stiffness of the structure decreases with the increasing amount
of the compatibilizer. If the reaction is allowed to continue, and there is no unreact-
ed polyamide left in the system, little or no thixotropy will be exhibited. Therefore,
the reaction must be precisely controlled to give the desired degree of thixotropy.
Aromatic solvents such as xylene tend to destroy the thixotropic structure. There-
fore, they must be reduced to less than 0.5% in the product. Polyamide modified
alkyd resins are available commercially to be used as additives for making thixotro-
pic alkyd paints.
7.2. High Solids Alkyds
There has been a strong trend in recent years to increase the solids level of all coat-
ing materials, including alkyds, to reduce solvent vapor emission. To raise the
solids level and still maintain a manageable viscosity, the molecular weight of
the resin must be reduced. Consequently, film integrity must be developed through
further chain extension and/or cross-linking of the resin molecules during the ‘‘dry-
ing’’ step. A high cross-linking density necessitated by the lower molecular weight
of the resin would build a high level of stress in the film, and cause it to be prone to
cracking. Therefore, adequate flexibility should be designed into the resin structure.
This means that the distance between the hydroxyl groups of the polyol and the
carboxyl groups of the dibasic acid would need to be lengthened by linear linkages.
Thus long-chain diols, polyether polyols, and linear a,o-dibasic acids would not
only build in more flexibility but also reduce the viscosity for high solids alkyds,
due to the greater spacing of polar ester groups and the reduction of aromaticity in
the resin structure. In addition to the manipulation of resin molecular structure for
increasing coating solids, the use of more active, though more expensive, oxyge-
nated solvents also serves to reduce the viscosity of resin solutions.
Chain extension and cross-linking of high solids alkyd resins are typically
achieved by the use of polyisocyanato oligomers or amino resins. An adequate
amount of excess hydroxyl groups must be designed into the alkyd structure to
provide reaction sites for these modifiers. To limit the molecular weight of the alkyd
resin, the molar ratio between polyols and dibasic acids should be greater than 1.
The hydroxyl functionality of the formulation should be controlled by a careful
selection of polyols to avoid an overpresence of free hydroxyl groups in the pro-
duct, which would adversely affect water resistance and other properties of the
coating film. Most of the high solids alkyd systems are used in industrial baking
finishes. For air drying applications, higher doses of driers are usually needed to
achieve acceptable drying rate (71).
MODIFICATION OF ALKYD RESINS BY BLENDING WITH OTHER POLYMERS 347
7.3. Water-Reducible Alkyds
Replacing solvent-borne coatings with water-borne coatings would not only reduce
solvent vapor emission but also improve safety against the fire and health hazards of
organic solvents. Alkyd resins may be rendered water-reducible by either convert-
ing the resin into an emulsion form or by incorporating ‘‘water-soluble’’ groups in
the molecules. The latter will be the subject for further discussion.
The most common approach for imparting water solubility in an alkyd resin is to
leave enough pendent carboxyl groups in the resin and to neutralize them with a
fugitive base, such as ammonia or low molecular weight amines, to build ionic char-
acteristics into the resin. Nonfugitive base materials, such as caustic soda, would
leave the salt in the coating film and damage its water- and corrosion-resistance.
Trimellitic anhydride (TMA) is the most frequent choice of ingredient to provide
the pendent carboxyl groups. It was reported that glycerol gives resins with poor
hydrolytic stability (72). Therefore, polyols with primary hydroxyl groups are pre-
ferred for the preparation of water-soluble alkyds.
The recommended procedure (37) for the preparation of water-soluble alkyds is
to hold off the TMA in the initial stage of the alkyd reaction so that the high func-
tionality of TMA would not be a cause of gelation. When the reaction has pro-
gressed to a desired low acid number, i.e., the building of the polymer chain is
completed, the temperature is lowered to 180�C; the TMA is then added and main-
tained at that temperature until a desired acid number, usually about 50–60, is
reached. At such a temperature, only the anhydride group of the TMA would react
to form half esters, and the remaining two carboxyl groups would essentially
remain unreacted. If one desires to have the TMA participating in the backbone
structure of the resin, a part of the TMA is charged in the beginning of the alkyd
reaction, often with the presence of an appropriate amount of a monohydric alcohol,
such as benzyl alcohol, to balance the functionality of the system. The remaining
TMA is then added in the same manner as described to ‘‘end cap’’ the resin and to
provide pendent carboxyl groups for water solubilization.
The finished resins are usually dissolved in oxygenated coupling solvents, such
as glycol ethers, to improve the solubilization of the resin in aqueous media and the
handling of the resin. Water and the base are premixed and added to the resin solu-
tion when needed. The coupling solvents usually have higher boiling points than
water. During the drying process, the solvent would be enriched in the coating
film as water evaporates preferentially. The resin molecules would become better
solubilized, i.e., molecular chains would be extended, and result in better formation
and integrity of the film.
8. ECONOMIC ASPECTS
Alkyd resins as a family have remained the workhorse of the coatings industry for
decades. In the United States, the total consumption of alkyds increased from about
200,000 t in the mid-1950s to more than 300,000 t in the mid-1960s. It peaked in
348 PAINTS, VARNISHES, AND RELATED PRODUCTS
1973 at about 345,000 t, constituting about 33% of all synthetic coating resins.
In 1980, alkyds still accounted for 30% of the 1,090,000 t of all resins consumed
for coatings. From 1987 to 1989, although the consumption maintained at about
300,000 t/year, its market share among all coating resins was reduced to 26% in
1987 and 25% in 1989. At present, 55–60% of the alkyd resins consumed in the
United States are used for architectural coatings. A decline in consumption is
expected because of regulations involving VOCs (volatile organic emissions). Cali-
fornia and the Northeastern United States are expected to adopt regulations that will
severely restrict the use of solvent-borne coatings (73).
The overall demand in Europe is expected to decrease at the rate of 3%/yr over
the next five years. Environmental regulations are expected by 2007. Japan’s con-
sumption has declined, but has stabilized because high performance alternatives
have already replaced the coatings in question.
The industry was hard hit in 2003–2004 with higher prices for raw materials
such as linseed and soybean oil. Alkyd producers are already developing new
water-borne products (73).
Other uses for alkyds are in general industrial coatings such as machinery and
metal furniture. Alkyd resin-chlorinated rubber based coatings are used in traffic
paints, but use is declining because of VOC concerns. Some alkyds are still used
in refinish paints for automobiles. Uralkyds are used as a vehicle for urethane
varnishes for the do-it-yourself market.
9. FUTURE PROSPECTS
Stemming from the drive by the coatings industry to reduce solvent emission, there
has been a clear trend of gradual decline in the market share of alkyd resins. How-
ever, their versatility and low cost will undoubtedly continue to keep alkyds as
major players in the coatings arena. Alkyds are much more amenable to move to-
ward higher solids than most other coating resins. Great strides in the development
of water-borne types have also been made in recent years. There is one more good
reason to remain optimistic about alkyds for the future—a significant portion of
their raw material, fatty acids, is renewable.
REFERENCES
1. A. E. Rheineck, J. Paint Technol. 44(566), 35–54 Apr. 1972.
2. A History of Paint and Color, Pittsburgh Plate Glass Co., 1951.
3. An Overview of the Paint and Coatings Industry, SRI International, Aug. 1992.
4. D. Deffar and M. D. Soucek, J. Coat. Technol, 73 (919), 95 (2001).
5. Urethane Surface Coatings, SRI Consulting, Oct. 2004.
6. Epoxy Surface Coatings, SRI Consulting, Oct. 2004.
7. Z. W. Wicks, Jr. and F. N. Jones in Z. W. Wicks, F. N. Jones, and S. P. Pappas, eds., Organic
Coatings Science & Technology, Vol. 1, John Wiley & Sons, Inc., New York, 1992, Chapt. 9.
REFERENCES 349
8. A. E. Rheineck and R. O. Austin in R. R. Meyers and J. S. Long, eds., Treatise on
Coatings, Vol. 1, Part 2, Marcel Dekker, Inc., New York, 1968, Chap. 4.
9. D. N. Rampley and J. A. Hasnip, J. Oil Colour Chem. Assoc. 59, 356–362 (1976).
10. O. S. Privett, W. O. Lundberg, N. A. Khan, W. E. Tolberg, and D. H. Wheeler, J. Am. Oil
Chem. Soc. 30, 61, (1953).
11. S. A. Harrison and D. H. Wheeler, J. Am. Chem. Soc. 76, 2379 (1954).
12. O. S. Privett and C. J. Nickell, J. Am. Oil Chem. Soc. 33, 156 (1956).
13. W. J. Bailey and G. L. Barlow, J. Paint Technol. 42(544), 287 (1970).
14. E. H. Farmer and A. Sundralingam, J. Chem. Soc. 1942, 121.
15. E. H. Farmer and D. A. Sutton, J. Chem. Soc. 1942, 139.
16. J. L. Bolland and G. Gee, Trans. Faraday Soc. 42, 236, 244 (1946).
17. E. H. Farmer, Trans. Faraday Soc. 42, 228 (1946).
18. E. H. Farmer, Trans. Inst. Rubber Ind. 21, 122 (1945).
19. F. D. Gunstone and T. P. Hilditch, J. Chem. Soc. 1946, 1022.
20. N. A. Khan, Can. J. Chem. 32, 1149 (1954).
21. N. Uri in W. O. Lunberg, ed., Autoxidation and Antioxidants, Vol. 1, Wiley-Interscience,
New York, 1961, Chapt. 2.
22. F. W. Heaton and N. Uri, J. Lipid Res. 2, 152 (1961).
23. T. H. Smouse and S. S. Chang, J. Am. Oil Chem. Soc. 44, 509 (1967).
24. H. P. Kaufmann, Fette Seifen Anstrichmit. 59, 153–162 (1957).
25. O. S. Privett, J. Am. Oil Chem. Soc. 36, 507 (1959).
26. R. N. Faulkner, J. Appl. Chem. 8, 448–458 (1958).
27. R. R. Allen and F. A. Kummerow, J. Am. Oil Chem. Soc. 28, 101 (1951).
28. A. E. Rheineck and S. C. G. Peng, Official Digest 36, 878 (1964).
29. L. A. O’Neill, Chem. Ind. 1954, 384–387.
30. K. Hultzsch, J. Prakt. Chem. 158, 275 (1941).
31. R. H. Kienle and C. S. Ferguson, Ind. Eng. Chem. 21, 349 (1929).
32. R. H. Kienle, Ind. Eng. Chem. 41, 726 (1949).
33. R. G. Mraz and R. P. Silver in Encyclopedia of Chemical Technology, 2nd ed., Vol. 1, John
Wiley & Sons, Inc., New York, 1963, pp. 851–880.
34. Z. W. Wicks, Jr., in Encyclopedia of Chemical Technology, 5th ed., Vol. 2, John Wiley &
Sons, Inc., Hoboken, New Jersey, 2004, pp. 147–169.
35. C-D-I-C Society for Paint Technology, Official Digest 430, 1477 (Nov. 1960).
36. Bulletin IP4, Amoco Chemicals Corp., Chicago, Oct. 1960.
37. Bulletin IP-65b, Amoco Chemicals Corp., Chicago, 1990.
38. Technical Bulletin No. 524-5, Velsicol Chemical Corp., Chicago.
39. R. I. Stirton in Encyclopedia of Chemical Technology, 1st ed., p. 595, Interscience
Publishers, New York, 1953.
40. Bulletin TMA 27, Amoco Chemicals Corp., Chicago.
41. IMC Polyols: A Complete Guide, International Minerals & Chemicals Corp., Des Plaines,
Ill., 1980, p. 9.
42. Trimethylolpropane in Alkyd Coating Resins, Celanese Chemical Co., New York, 1961, p. 4.
350 PAINTS, VARNISHES, AND RELATED PRODUCTS
43. L. Klee and G. H. Benham, J. Am. Oil Chem. Soc. 27, 130–133 (1950).
44. A. E. Rheineck, F. D. Williamson, and D. DeClerk, Am. Chem. Soc. Div. Org. Coat. Plast.
Chem. 22(1), 24–34 (1962).
45. W. H. Carothers, J. Am. Chem. Soc. 51, 1548 (1929).
46. P. J. Flory, Principles of Polymer Chemistry, Cornell University Press, Ithaca, N.Y., 1953,
Chapt. 9.
47. W. H. Carothers, Trans Faraday Soc. 32, 43 (1936).
48. T. C. Patton, Alkyd Resin Technology, Formulating Techniques and Allied Calculations,
Wiley Interscience, New York, 1962.
49. E. G. Bobalek, E. R. Moore, S. S. Levy, and C. C. Lee, J. Appl. Polym. Sci. 8, 625–657
(1964).
50. D. H. Solomon, B. C. Loft, and J. D. Swift, J. Appl. Polym. Sci. 11, 1593–1602 (1967).
51. D. H. Solomon and J. J. Hopwood, J. Appl. Polym. Sci. 10, 1893–1914 (1966).
52. J. Kumanotani, H. Hata, and H. Masuda, Org. Coat. 6, 35–54 (1984).
53. H. Kiryu, K. Horiuchi, K. Sato, and J. Kumanotani, Shikizai Kyokaishi 57(11), 597–601
(1984).
54. H. Hata, H. Tomita, Y. Nishizawa, and J. Kumanotani, Fatipec Cong. 15(3), 111-485/509
(1980).
55. H. Hata, J. Kumanotani, Y. Nishizawa, and H. Tomita, Fatipec Cong. 14, 359–364 (1978).
56. N. M. Wiederhorn, Am. Paint J. 41(2), 106 (1956).
57. R. P. Silver, Alkyd Report No. 8, Hercules Inc., Wilmington, Del.
58. R. P. Silver, Alkyd Report No. 1.2, Hercules Inc., Wilmington, Del.
59. T. C. Patton, Off. Digest Fed. Paint Varnish Prod. Clubs 430, 1544 (1960).
60. Y. Tanizaki and T. Yoshida, Shikizai Kyokaishi 45(2), 83–87 (1972).
61. T. Nagata, J. Appl. Polym. Sci. 13, 2601–2619 (1969).
62. T. Yoshida, Kobunshi Kagagu 22, 769 (1965).
63. Alkyd Report No. 1.5, Hercules Inc., Wilmington, Del.
64. L. W. Chen and J. Kumanotani, J. Appl. Polym. Sci. 9, 3649–3660 (1965).
65. W. M. Kraft, G. T. Roberts, E. G. Janusz, and J. Weisfeld, Am. Paint J. 41(28), 96 (1957).
66. W. B. Callahan and B. F. Coe (to E. I. du Pont de Nemours & Co.), U.S. 4,045,932
(Aug. 30, 1977).
67. A. F. Karim, B. Golding, and R. A. Morgan, J. Chem. Eng. Data 5, 117 (1960).
68. Silicone Notes 7-701, 7-702a, 7-703, Technical Bulletin, Dow Corning Corp., Midland,
Mich.
69. A. G. North, J. Oil Color Chem. Assoc. 39(9), 696 (1956).
70. P. Oldring and G. Hayward, eds., Resins for Surface Coatings, SITATechnology, London,
1987.
71. J. Larson, Am. Paint Coat. J., 56–61 (Apr. 4, 1984).
72. M. Lerman, J. Coat. Technol. 48(12), 37–42 (1976).
73. Alkyd/Polyester Surface Coatings, SRI Consulting, Jan. 2005.
REFERENCES 351