Home

Lubrication Theory and Practice

Lubrication Theory and Practice

 

 

Lubrication Theory and Practice

Introduction

The basic functions of a lubricant are friction reduction, heat removal and suspension of contaminants. Designing a lubricant to perform these functions is a complex task, involving a careful balance of properties both in the base oil and the performance enhancing additives. This paper provides an overview of all the factors affecting proper lubricant performance, including a look at lubrication theory, base stock characteristics, additive design and function, and the needs of various end use applications.

Friction Reduction

Simply stated, friction is reduced by maintaining a film of lubricant between surfaces that are moving with respect to each other, thereby preventing the surfaces from coming into contact and subsequently causing surface damage. Friction is a common element in daily life. One can walk up a steep ramp without slipping back because of high friction between shoe soles and the ramp surface. One can slide down a ski run because friction between packed snow and skis is low. Both cases illustrate friction between ordinary surfaces.
The amount of frictional resistance to motion can be expressed in terms of the coefficient of friction:


Friction Coefficient  =

Friction force opposing motion

-----------------------------------------

Load @ right angles to surfaces

The coefficient is roughly constant for any pair of surfaces. For nonlubricated metal of ordinary surface finish and cleanliness, exposed to the atmosphere, the value may be about 1. For the same metal contaminated by handling, the value will drop to about 0.3 to 0.1. For well-designed and well-lubricated systems, the coefficient may be as low as 0.005. Under very special conditions, values as low as 0.000005 have been attained. By contrast, the coefficient for clean metal surfaces in a vacuum may be as high as 100 to 200 or more, and cold welding due to adhesion can occur.
Lubrication is of two general types based on the operating environment; that is, load and speed of the equipment and viscosity of the lubricant. Smooth surfaces separated by a layer of lubricant do not come into contact and, hence, do not contribute to frictional forces. This condition is called hydrodynamic lubrication. Boundary lubrication, on the other hand, arises when there is intermittent contact between surfaces, resulting in significant frictional forces.
Hydrodynamic Lubrication
Keeping a liquid film intact between surfaces moving with respect to each other is generally done mechanically, as by pumping. In a cylindrical journal and bearing, the rotary shaft acts as a pump to maintain the lubricant film. The journal floats on a film of oil with an equilibrium thickness established between oil input and oil leakage (mostly at the bearing ends).
The equilibrium thickness of the oil film can be altered by:

  • Increasing load, which squeezes out oil.
  • Increasing temperature, causing more oil leakage.
  • Changing to a lower viscosity oil, which also causes more oil leakage.
  • Reducing journal speed, which generates a thinner oil film.

Lubrication of a journal rotating in a cylindrical bearing offers the classic example of the hydrodynamic theory of bearing friction, as described by Osborne Reynolds in 1886. The theory assumes that under these conditions, friction occurs only within the fluid film, and is a function of fluid viscosity.
Elastohydrodynamic Lubrication
As pressure or load increases, viscosity of the oil also increases. As the lubricant is carried into the convergent zone approaching the contact area, the two surfaces deform elastically due to lubricant pressure. In the contact zone, the hydrodynamic pressure developed in the lubricant causes a further increases in viscosity that is sufficient to separate the surfaces at the leading edge of the contact area. Because of this high viscosity and the short time required to carry the lubricant through the contact area, the lubricant cannot escape, and the surfaces will remain separated.
Load has little effect on film thickness because at the pressures involved, the oil film is actually more rigid than the metal surfaces. Therefore, the main effect of a load increase is to deform the metal surfaces and increase the contact area, rather than decrease the film thickness.

Boundary Lubrication
The simple assumptions made in discussing fluid film lubrication are hardly ever valid in practice. Under certain conditions -- such as shock loading, steady heavy load, high temperature, slow speed, and critically low viscosity -- the lubricant system no longer remains in the hydrodynamic regime. A situation arises wherein there is intermittent contact between the surfaces, resulting in a significant rise in temperature and subsequent destruction of the contacting surfaces. Under these circumstances, the fluid film is no longer capable of adequately protecting the surfaces, and other approaches must be employed such as adding film-forming additives.
Lubricant Viscosity
Viscosity is one of the most important properties of a lubricating oil. It is one factor responsible for the formation of lubricating films under both thick and thin film conditions. Viscosity affects heat generation in bearings, cylinders and gears due to internal fluid friction. It affects the sealing properties of oils and the rate of oil consumption. It determines the ease with which machines can be started at various temperatures, particularly cold temperatures. The satisfactory operation of any given piece of equipment depends on using an oil with the proper viscosity at the expected operating conditions.
Lubrication TheoryThe basic concept of viscosity is shown in the figure, where a plate is being drawn at uniform speed over a film of oil. The oil adheres to both the moving and stationary surfaces. Oil in contact with the moving surface travels at the same velocity, V, as that surface, while oil in contact with the stationary surface is at zero velocity. In between, the oil film can be visualized as many layers, each being drawn by the layer above it at a fraction of velocity V proportional to its distance above the stationary plate.
A force F must be applied to the moving plate to overcome the friction between the fluid layers. Since this friction is related to viscosity, the force necessary to move the plate is proportional to viscosity. Viscosity can be determined by measuring the force required to overcome fluid friction in a film of known dimensions. Viscosity determined in this manner is called dynamic or absolute viscosity.
Dynamic viscosity is usually reported in poise (P) or centipoise (cP, where 1 cP = 0.01 P), or in SI units as pascal-seconds (Pa-s, where 1 Pa-s = 10 P). Dynamic viscosity, which is a function of only the internal friction of a fluid, is the quantity used most frequently in bearing design and oil flow calculations.
Because it is more convenient to measure viscosity in a manner such that the measurement is affected by oil density, kinematic viscosity is normally used to characterize lubricants. Kinematic viscosity of a fluid equals its dynamic viscosity divided by its density, both measured at the same temperature and in consistent units. The most common units for reporting kinematic viscosity are stokes (St) or centistokes (cSt, where 1 cSt = 0.01 St), or in SI units as square millimeters per second (mm2/s, where 1 mm2/s = 1 cSt).
Dynamic viscosity in centipoise can be converted to kinematic viscosity in centistokes by dividing by the fluid density in grams per cubic centimeter (g/cm3) at the same temperature. Kinematic viscosity in square millimeters per second can be converted to dynamic viscosity in pascal-seconds by multiplying by the density in grams per cubic centimeter and dividing the result by 1000.
In summary,

 

 

Force

 

dynes

 

 

Shear Stress

=

-------------

=

--------

 

 

 

 

Area

 

cm2

 

 

 

 

 

 

 

 

 

 

 

Fluid Velocity

 

cm/s

 

 

Shear Rate

=

-------------------

=

----------

=

s-1

 

 

Gap

 

cm

 

 

 

 

 

 

 

 

 

 

 

Shear Stress

 

dynes/cm2

 

 

Absolute Viscosity

=

----------------------

=

----------------

=

1 P

 

 

Shear Rate

 

s-1

 

 

 

 

 

 

 

 

 

1 P = 100 cP

 

100 P = 1 Pa-s

 

 

 

 

 

 

 

 

 

 

 

 

 

Absolute Viscosity

 

 

 

 

Kinematic Viscosity

=

----------------------

=

1 Stoke

 

 

 

 

Density

 

 

 

 

Other viscosity systems, including Saybolt, Redwood, and Engler, have also been used because of their familiarity to many people. The instruments developed to measure viscosity in these systems are rarely used. Most viscosity determinations are made in centistokes and converted to values in other systems.
The viscosity of any fluid changes with temperature, increasing as temperature decreases, and decreasing as temperature rises. Viscosity may also change with a change in shear stress or shear rate.
To compare petroleum base oils with respect to viscosity variations with temperature, ASTM Method D 2270 provides a means to calculate a viscosity index (VI). This is an arbitrary number used to characterize the variation of kinematic viscosity of a petroleum product with temperature. The calculation is based on kinematic viscosity measurements at 40 and 100°C. For oils of similar kinematic viscosity, the higher the viscosity index, the smaller the effect of temperature.
The benefits of higher VI are: 1. Higher viscosity at high temperature, which results in lower engine oil consumption and less wear. 2. Lower viscosity at low temperature, which for an engine oil may result in better starting capability and lower fuel consumption during warm-up.
The measurement of absolute viscosity under realistic conditions has replaced the conventional viscosity index concept in evaluating lubricants under operating conditions.
Another factor in viscosity measurements is the effect of shear stress or shear rate. For certain fluids, referred to as Newtonian fluids, viscosity is independent of shear stress or shear rate. When viscosity is affected by changes in shear stress/shear rate, the fluid is considered non-Newtonian.
Kinematic viscosity measurements are made at a low shear rate (100 s-1). Other methods are available to measure viscosity at shear rates that simulate the lubricant environment under actual operating conditions. Different instruments used to measure kinematic viscosity are:
1. Capillary Viscometers measure the flow rate of a fixed volume of fluid through a small orifice at a controlled temperature. The rate of shear can be varied from near zero to 106 s-1 by changing capillary diameter and applied pressure. Types of capillary viscometers and their mode of operation are:
Glass Capillary Viscometer — Fluid passes through a fixed-diameter orifice under the influence of gravity. The rate of shear is less than 10 s-1. All kinematic viscosities of automotive fluids are measured by capillary viscometers.
High-Pressure Capillary Viscometer — Applied gas pressure forces a fixed volume of fluid through a small-diameter glass capillary. The rate of shear can be varied up to 106 s-1. This technique is commonly used to simulate the viscosity of motor oils in operating crankshaft bearings. This viscosity is called high-temperature high-shear (HTHS) viscosity and is measured at 150°C and 106 s-1. HTHS viscosity is also measured by the Tapered Bearing Simulator (see below).
2. Rotary Viscometers use the torque on a rotating shaft to measure a fluid's resistance to flow. The Cold Cranking Simulator (CCS), Mini-Rotary Viscometer (MRV), Brookfield Viscometer and Tapered Bearing Simulator (TBS) are all rotary viscometers. Rate of shear can be changed by changing rotor dimensions, the gap between rotor and stator wall, and the speed of rotation.
Cold Cranking Simulator — The CCS measures an apparent viscosity in the range of 500 to 200,000 cP. Shear rate ranges between 104 and 105 s-1. Normal operating temperature range is 0 to -40°C. The CCS has demonstrated excellent correlation with engine cranking data at low temperatures. The SAE J300 viscosity classification specifies the low-temperature viscometric performance of motor oils by CCS limits and MRV requirements.
Mini-Rotary Viscometer (ASTM D 4684) — The MRV test, which is related to the mechanism of pumpability, is a low shear rate measurement. Slow sample cooling rate is the method's key feature. A sample is pretreated to have a specified thermal history which includes warming, slow cooling, and soaking cycles. The MRV measures an apparent yield stress, which, if greater than a threshold value, indicates a potential air-binding pumping failure problem. Above a certain viscosity (currently defined as 60,000 cP by SAE J 300), the oil may be subject to pumpability failure by a mechanism called "flow limited" behavior. An SAE 10W oil, for example, is required to have a maximum viscosity of 60,000 cP at -30°C with no yield stress. This method also measures an apparent viscosity under shear rates of 1 to 50 s-1.
Brookfield Viscometer — Determines a wide range of viscosities (1 to 105 P) under a low rate of shear (up to 102 s-1). It is used primarily to determine the low-temperature viscosity of automotive gear oils, automatic transmission fluids, torque converter and tractor fluids, and industrial and automotive hydraulic fluids. Test temperature is held constant in the range -5 to -40°C.
The Scanning Brookfield technique measures the Brookfield viscosity of a sample as it is cooled at a constant rate of 1°C/hour. Like the MRV, this method is intended to relate to an oil's pumpability at low temperatures. The test reports the gelation point, defined as the temperature at which the sample reaches 30,000 cP. The gelation index is also reported, and is defined as the largest rate of change of viscosity increase from -5°C to the lowest test temperature. This method is finding application in engine oils, and is required by ILSAC GF-2.
Tapered Bearing Simulator — This technique also measures high-temperature high-shear rate viscosity of motor oils (see High Pressure Capillary Viscometer). Very high shear rates are obtained by using an extremely small gap between the rotor and stator wall.
Physical requirements for both crankcase oils and gear lubricants are defined by SAE J300.
Heat Removal
Another important function of a lubricant is to act as a coolant, removing heat generated by either friction or other sources such as combustion or contact with high-temperature substances. In performing this function, the lubricant must remain relatively unchanged. Changes in thermal and oxidative stability will materially decrease a lubricant's efficiency in this regard. Additives are generally employed to solve such problems.
Suspension of Contaminants
The ability of a lubricant to remain effective in the presence of outside contaminants is quite important. Among these contaminants are water, acidic combustion products, and particulate matter. Additives are generally the answer in minimizing the adverse effects of contaminants.

 

 

Lubricant Base Stocks

A lubricant usually consists of a base fluid, generally of petroleum origin, combined with additive chemicals that enhance the various desirable properties of the base fluid. Base fluids are essentially obtained from two main sources: the refining of petroleum crude oil and the synthesis of relatively pure compounds with properties that are suitable for lubricants.
Petroleum Base Oils
Petroleum was formed many millions of years ago. It is believed to originate from the remains of tiny aquatic animals and plants that settled with mud and silt to the bottoms of ancient seas. As successive layers built up, the deposits were subjected to high pressures and temperatures and, as a result, underwent chemical transformations, leading to the formation of the hydrocarbons and other constituents of crude oil. In many areas, the crude oil migrated and accumulated in porous rocks overlaid by impervious rock that prevented further movement. Usually, a layer of concentrated salt water underlies the oil pool.
Crude oil is recovered by drilling holes as deep as five miles into the earth's crust. The crude oil frequently comes to the surface under great pressure and in combination with large volumes of gas. The gas is separated from the oil and processed to remove liquids of high volatility, which constitute "natural gasoline." The dry gas is sold as fuel or recycled back to the underground formations to maintain pressure in the oil pool and, thus, increase crude oil recovery.
Crude oils are found in a variety of types, ranging from light-colored oils (consisting mainly of gasoline) to black, nearly solid asphalts. These crudes are highly complex mixtures containing many hydrocarbons, ranging from methane — the main constituent of natural gas with one carbon atom — to compounds containing fifty or more carbon atoms.

Lubricant Base Stocks

The boiling range of a compound increases roughly with an increase in the number of carbon atoms:


Components

Approximate Boiling Range (°C)

Natural Gas Hydrocarbons

Below -20

Gasoline Components

30 to 200

Diesel and Home Heating Oils

200 to 350

Lubricating Oils and Heavier Fuels

Above 350

The heavier asphaltic materials cannot be vaporized because they decompose when heated above normal distillation temperatures, and their molecules either "crack" to form gas, gasoline and lighter fuels, or unite to form higher molecular weight molecules. These latter materials result in carbonaceous residues called "coke."
Crude oils also contain varying amounts of compounds of sulfur, nitrogen, and oxygen; metals such as vanadium and nickel; water; and salts. All of these materials can cause problems in refining or subsequent product applications. Their reduction or removal increases refining cost appreciably.
The first step in petroleum refining is usually a desalting operation, followed by heating in a furnace where the oil is partially vaporized. The mixture of hot liquid and vapor enters a fractionating column operating at slightly above atmospheric pressure. This device separates groups of hydrocarbons according to their boiling range. A heavy black residuum is drawn from the bottom of the atmospheric tower.
Because the residuum tends to decompose at temperatures above 700°F (371°C), higher boiling oils such as lubricating oils must be distilled off in a separate vacuum fractionating tower. The greatly reduced pressure in the tower markedly lowers the boiling points of the desired oil compounds. Bottom materials from the vacuum tower are either used for asphalt or are further processed for other materials such as bright stocks. The fractions separated by crude distillation are referred to as "straight run" products.
Petroleum lubricating oils are made from the higher boiling portion of the crude oil that remains after removal of the lighter fractions. They are prepared from crude oils obtained from most parts of the world. These crude oils differ widely in properties. An example of the complexity of the lubricating oil refining problem is the variation that can exist in a single hydrocarbon molecule with a specific number of carbon atoms. A paraffinic molecule with 25 carbon atoms, representing a compound falling well within the normal lubricating oil range, would have 52 hydrogen atoms and could have about 37 million different molecular arrangements.
Considering that some naphthenic and aromatic hydrocarbon molecules also have 25 carbon atoms, the number of possible variations in molecular arrangements is immense. This accounts for much of the possible variation in physical characteristics and performance qualities of base oils prepared from different crude sources.
The manufacture of lube base stocks from crude oil involves a series of subtractive processes to remove undesirable components, resulting in a base oil that meets performance requirements. Essentially five steps are involved:
1. Vacuum distillation, which separates the atmospheric residue mixture into a series of fractions representing different molecular weight ranges or viscosity ranges from the 90-100 neutrals to the 500 neutrals. (The neutral number is the SUS viscosity at 100°F). The residue contains the heavier base oils such as the bright stocks (150 to 250 SUS at 210°F). The latter must be separated from the asphaltenes and resins prior to introduction into the extraction process.
2. Solvent extraction (furfural in this case) separates aromatic compounds from nonaromatic compounds. In its simplest form, the process consists of mixing furfural with the feedstock and allowing the mixture to settle into two phases, the extract and the raffinate. The two layers are separated, and the solvent is removed from each phase.
The extract phase is rich in aromatics, and the raffinate phase is rich in paraffinic hydrocarbons. The extraction process improves thermal and oxidative stability compared to the fraction prior to extraction. In addition, the viscosity/temperature characteristics improve, as evidenced by a higher viscosity index.
3. The next step in lube oil manufacture is the removal of wax to improve its flow characteristics at low temperature. Typically, methyl ethyl ketone (MEK) is mixed with the waxy oil. The mixture is then cooled to a temperature 10 to 20°F (-12 to -6°C) below the desired pour point. The wax crystals that form are then removed from the oil by filtration.
4. Some base stocks, particularly premium stocks, require a finishing process such as hydrofinishing or clay treatment to improve color, oxidation stability, and thermal stability. Hydrofinishing consists of passing heated oil and hydrogen through a catalyst bed. The process removes some color bodies and unstable components, such as nitrogen and sulfur compounds. An alternative process, clay treatment, also removes dark colored and unstable molecules.
Several hydrogen processes have been used in addition to hydrofinishing. Hydrotreating, a more severe process, is sometimes used prior to solvent extractions. The objective is to improve the yield from the extraction process by converting some aromatic molecules, which would end up in the extract, into nonaromatic molecules that will remain in the raffinate. This process usually results in a high degree of desulfurization as well as moderate nitrogen removal.
5. A totally different approach to lube oil manufacture involves an even more severe hydrogen process called hydrocracking. This process changes the structure of many of the molecules in the feedstock. Aromatics are converted into naphthenes, many naphthene rings are broken open, and many paraffinic molecules are rearranged or fragmented. This massive "reforming" of the feedstock produces molecules that have improved viscosity/temperature characteristics and improved thermal and oxidative stability. This process allows a great deal of flexibility relative to crude source for the production of high-quality lube stocks.
To minimize variations and produce products what will provide consistent performance, the refiner exercises care in: 1. Selection and segregation of crudes. 2. Separation into similar fractions in the same general boiling range. 3. Processing to remove undesirable constituents and upgrading into more desirable materials. 4. Blending to the required physical characteristics and incorporation of chemical additives that improve performance.
The table below shows some inspection characteristics of finished petroleum base oils obtained from various crude oils using the processes described above.
Inspection Characteristics of Some Finished Petroleum Oils

 

Specific Gravity at 60°F

Sulfur (% wt)

Viscosity Index

Kinematic Viscosity (cSt)

Pour Point (°C)

COC Flash (°C)

at 40°C

at 100°C

Source 1

100 Neutral

0.860

0.065

101

20.39

4.11

-13

192

200 Neutral

0.872

0.096

99

40.74

6.23

-20

226

350 Neutral

0.877

0.126

97

65.59

8.39

-18

252

650 Neutral

0.882

0.155

96

117.90

12.43

-18

272

150 Bright
Stock

0.895

0.263

95

438.00

29.46

-18

302

Source 2

150 Neutral

0.861

0.036

98

24.38

4.55

-23

210

250 Neutral

0.872

0.055

96

48.96

6.94

-21

238

600 Neutral

0.878

0.099

95

108.00

11.64

-23

262

150 Bright
Stock

0.892

0.147

95

473.00

30.90

-15

294

Source 3 (Hydrotreated)

100 Neutral

0.868

0.018

100

25.18

4.66

-20

200

200 Neutral

0.869

0.012

101

39.78

6.19

-21

216

500 Neutral

0.869

0.015

105

89.37

10.78

-21

254

Source 4

100 Neutral

0.862

0.278

107

21.26

4.28

-16

186

200 Neutral

0.877

0.571

103

30.53

5.26

-13

194

500 Neutral

0.888

0.729

98

95.48

10.89

-10

244

600 Neutral

0.891

0.760

96

111.80

11.99

-13

258

150 Bright
Stock

0.903

0.843

96

477.80

30.99

-13

290

Synthetic Base Oils
Another source of lubricant base fluids is the synthetic route. A suitable definition for such a material is "A product prepared by chemical reaction of lower molecular weight materials to produce a fluid of higher molecular weight designed to provide certain predictable properties." This is in contrast to refined petroleum oils, which are composed of many compounds of varying chemical composition, depending on the refining method and the crude stock source.
Among the advantages claimed for synthetic lubricants over comparable petroleum-based fluids are improved thermal and oxidative stability, more desirable viscosity/temperature characteristics, improved low-temperature properties, superior volatility characteristics, and preferred frictional properties. Commercial synthetic fluids are not confined to a single chemical type. Among those of current commercial interest are :

  • Olefin oligomers — Automotive and industrial applications
  • Neopentyl polyol esters — Automotive and aircraft applications
  • Esters of dibasic acids — Automotive and aircraft applications
  • Alkylated aromatics — Automotive and industrial applications

These four types have found use in automotive lubricants, either alone or in combination with petroleum base oils. The table below lists some inspection characteristics of synthetic fluids together with the applicable temperature range.
Physical Inspection Characteristics of Typical Synthetic Fluids


Fluid

Dynamic Viscosity (cP) at -40°F

Kinematic Viscosity (cSt)

Viscosity Index

Pour Point (°C)

COC Flash (°C)

Temperature Range (°C)

at 40°C

at 100°C

Olefin Oligomer

2371

18.12

3.96

126

-79

221

-65 to 232

Olefin Oligomer

8176

34.07

6.00

134

-68

243

-65 to 232

Ester of Dibasic Acid — Dioctyl Sebacate

3450

119.58

76

-51

232

-54 to 204

Ester of Trimethylol — Propane (C7)

2360

15.00

3.50

< -51

232

-59 to 280

Alkylated Aromatics

9047

29.37

5.10

119

-54

224

-40 to 177

Other fluids find niche uses in very specialized applications. These include polyglycols, phosphate esters, silicones, silicate esters, and polyphenyl ethers.
Synthetic materials, in general, can be used over a wider temperature range than petroleum base fluids in the same viscosity range. Certain synthetic lubricant base stocks can be blended with petroleum oils to obtain necessary high-temperature volatility and low-temperature viscosity characteristics when the proper petroleum base oils are unavailable.

Lubricant Properties and the Role of Additives

 

Some of the most important properties necessary for satisfactory lubricant performance are:
1. Low volatility under operating conditions. Volatility characteristics are essentially inherent in the choice of base oil for a particular type of service and cannot be improved by the use of additive materials.
2. Satisfactory flow characteristics in the temperature range of use. Flow characteristics largely depend on the choice of base oil; however, they can be improved through the use of pour point depressants and viscosity modifiers. The former improve low-temperature flow properties, while the latter enhance high-temperature viscosity characteristics.
3. Superior stability or ability to maintain desirable characteristics for a reasonable period of use. While these characteristics depend to some extent on the base oil, they are primarily associated with additive materials, which enhance base fluid properties in this area.
Lubricant stability is affected by the environment in which it operates. Such factors as temperature, oxidation potential and contamination with water, unburned fuel fragments, and corrosive acids limit the useful life of a lubricant. This is the area where additives have made a major contribution in improving the performance characteristics and extending the useful life of lubricants.
4. Compatibility with other materials in the system. Compatibility of lubricants with seals, bearings, clutch plates, etc., may also be partially associated with the base oil. However, additive chemistry can have a major influence on such characteristics.
Additives can be classified as materials that impart new properties to or enhance existing properties of the lubricant or fuel into which they are incorporated. It is not the object of this presentation to give a complete bibliography of the literature pertaining to these materials. An attempt will be made to present an overview of the field both as to chemistry and function.
The principal types of engine lubricant additives have been described in the literature by various authors. Materials of current interest in this area include:
Lubricant Additive Types


Detergents (Metallic Dispersants)

Salicylates
Sulfonates
Phenates
Sulfophenates

Ashless Dispersants

N-substituted long-chain alkenyl succinimides
High-molecular-weight esters and polyesters
Amine salts of high-molecular-weight organic acids
Mannich base derived from high-molecular-weight alkylated phenols
*Copolymers of methacrylic or acrylic acid derivatives containing polar groups such as amines, amides, imines, imides, hydroxyl, ether, etc.
*Ethylene-propylene copolymers containing polar groups as above

Oxidation and Bearing Corrosion Inhibitors

Organic phosphites
Metal dithiocarbamates
Sulfurized olefins
Zinc dithiophosphates

Antioxidants

Phenolic compounds
Aromatic nitrogen compounds
Phosphosulfurized terpenes

Viscosity Modifiers

Polymethacrylates
Ethylene-propylene copolymers (OCP)
Styrene-diene copolymers
Styrene-ester copolymers

Antiwear Additives

Organic phosphites
Sulfurized olefins
Zinc dithiophosphates
Alkaline compounds as acid neutralizers

Pour Point Depressants

Wax alkylated naphthalene
Polymethacrylates
Crosslinked wax alkylated phenols
Vinyl acetate/fumaric-acid-ester copolymers
Vinyl acetate/vinyl-ether copolymers
Styrene-ester copolymers

*Also viscosity modifiers
Detergents
Materials of this type are generally molecules having a large hydrocarbon "tail" and a polar head group. The tail section, an oleophilic group, serves as a solubilizer in the base fluid, while the polar group is attracted to contaminants in the lubricant.
Although these compounds are commonly called detergents, their function appears to be the dispersing of particulate matter rather than cleaning up existing dirt and debris. Therefore, it is more appropriate to categorize them as dispersants. The molecular structure and a brief outline of the preparation methods for some representative types of metallic dispersants are discussed below.
Sulfonates
Sulfonates are the products of the neutralization of a sulfonic acid with a metallic base. The reaction can be illustrated as:
Lubricant Properties
where MO = divalent metal oxide and MOH = divalent metal hydroxide. R represents the organic radical that acts as an oil solubilizing group.
The molecular weight of the hydrocarbon must be on the order of 350 or more, and the presence of the organic radical in the molecule is considered necessary for the oil solubility of the sulfonate. Commercially available sulfonates are of two types: petroleum sulfonates and synthetic sulfonates.
Petroleum (or natural) sulfonates are metal salts of sulfonic acids that were formerly byproducts of the sulfuric acid treatment of oil fractions in the manufacture of white oils. Currently, with the high demand for detergent oils, sulfonates rather than white oils have become the principal product. The structure of the organic portion of petroleum sulfonates is not completely known. Depending on the crude oil source, the structure can have varying proportions of aliphatic, naphthenic, and aromatic hydrocarbon groups.
Synthetic sulfonates are metal salts of acids produced from the sulfonation of alkylated aromatics by reaction with sulfur trioxide. In many cases, synthetic sulfonates were derivatives of benzene with long alkyl substituents, whose structure is illustrated at left, where R and R' are aliphatic radicals with a combined carbon number over C20.
Lubricant Properties
Most metallic cations of sulfonate detergents are calcium, magnesium, and sodium. Alkaline-earth sulfonates can be prepared by direct reaction of sulfonic acid with the metal oxide or hydroxide, or by reacting the sodium sulfonate with the metal chloride.
Oil-soluble sulfonates containing metal in excess of the stoichiometric amount are called basic sulfonates. Among the advantages of basic sulfonates is a greater ability to neutralize acidic bodies in addition to serving as a dispersant for contaminants.
Salicylates
Salicylates are generally prepared from alkyl phenols by a chemical scheme known as the Kolbe reaction.
Lubricant Properties
The potassium salicylate may be metathesized with calcium chloride or magnesium chloride. The resulting salts are then overbased to form highly basic detergents that have proven effective in diesel engine oil formulations.
Phenates and Phenol Sulfide Salts
The broad class of metal phenates includes the salts of alkylphenols, alkylphenol sulfides, and alkylphenol aldehyde products. Oil solubility is provided by alkylating the phenol with olefins that generally contain seven or more carbon atoms.
Lubricant Properties
Sulfur is incorporated into the phenates by reacting the alkylphenol with sulfur chloride or elemental sulfur. The introduction of sulfur and the presence of a methylene bridge lowers the corrosivity of the products toward bearing materials and improves their antioxidant characteristics.
Calcium phenates are currently the most widely used types. They are manufactured by reacting the substituted phenols with the oxides or hydroxides of the metals. Basic phenates can be produced by using an excess of the metal base over the theoretical amounts required to form neutral phenates. Basic phenates have greater acid neutralization potential per unit of weight. Such products have two to three times the amount of metal required for neutral phenates.
In the structures for the various phenates shown, M = divalent metal and R = alkyl group.
Lubricant Properties
Thiophosphonates
Commercial products of this type are generally derived from acidic components produced by the reaction between polybutene (500 to 1000 molecular weight range) and phosphorus pentasulfide. A study of the structure of these compounds indicated that the organic salts present are principally thiopyrophosphonates, accompanied in some cases by 10 to 25 mole per cent of thiophosphonates and phosphonates. Oil-soluble phosphonates and thiophosphonates that contain metal in excess of the stoichiometric amount can also be prepared. However, these materials have almost vanished from use.
Dispersants
A major development in the additive field was the discovery and use of ashless dispersants. These materials may be categorized into two broad types: high-molecular weight polymeric dispersants used to formulate multigrade oils and lower molecular weight additives for use where viscosity modification is not necessary. These additives are much more effective than the metallic types in controlling sludge and varnish deposits that result from intermittent and low-temperature gasoline engine operation.
Compounds useful for this purpose are again characterized by a polar group attached to a relatively high molecular weight hydrocarbon chain. The polar group generally contains one or more of the elements nitrogen, oxygen and phosphorus. The solubilizing chains are generally higher in molecular weight than those in detergents; however, they may be quite similar in some instances.
No attempt will be made to describe all the materials that fit into this category. The discussion will be limited to some of the more widely used commercial products.
N-Substituted Long-Chain Alkenyl Succinimides
The majority of products currently in use are of this type or related materials that correspond to the following general formula:
Lubricant Properties
The alkenylsuccinic acid intermediate is obtained by condensing an olefin polymer, generally a polyisobutylene with a molecular weight in the range of 800 to 1200, with maleic anhydride. The basic part of the additive usually results from N-amino alkylpolyamines, especially the polyalkylene amines such as triethylenetetramine, tetraethylene pentamine, etc.
High Molecular Weight Esters
Materials of commercial interest in this area include products formed by the esterification of olefin substituted succinic acids with mono or polyhydric aliphatic alcohols. The olefin substituent in the acids has at least 50 aliphatic carbon atoms and a molecular weight of about 700 to 5000. An example of such a material is the reaction product of ethylene glycol with a substituted succinic anhydride:
Lubricant Properties
Polyhydric alcohols such as glycerol, pentaerythritol and sorbitol may be employed in such a reaction.
Mannich Bases from High Molecular Weight Alkylated Phenols
Such products are formed by the condensation of a high molecular weight alkyl-substituted phenol, an alkylenepolyamine, and an aldehyde such as formaldehyde. A description of the reaction product from polypropylenephenol, tetraethylenepentamine, and formaldehyde is:
Lubricant Properties
Polymeric Dispersants
These ashless dispersants may serve the dual function of dispersant and viscosity modifier. They have two different structural features: those that are similar to materials employed as viscosity modifiers and those of polar compounds (which impart dispersancy). The viscosity modifiers will be discussed in a separate section. The general formula for dispersant polymers might be:
Lubricant Properties
where the hydrocarbon portion is the oleophilic group, A = polar group, and R = hydrogen C1-6 alkyl, C4-6 alkenyl, or alkyl. Some of the many possibilities for the polar groups are:
Lubricant Properties

Oxidation and Bearing Corrosion Inhibitors
The function of an oxidation inhibitor is to prevent deterioration of the lubricant associated with oxygen attack. These inhibitors either destroy free radicals (chain breaking) or interact with peroxides involved in the oxidation mechanism. Among the widely used antioxidants are phenolic types and zinc dithiophosphates. The former are considered to be of the chain-breaking variety, whereas the latter are believed to be peroxide destroyers.
The corrosion of bearing metal is generally considered to be due largely to reaction of the acid with the oxides of the bearing metal. In engine operation, these acids either originate from products of incomplete fuel combustion that find their way into the lubricant as blowby gases or are produced from lubricant oxidation. Oxidation inhibitors can significantly reduce this tendency.
Detergents can reduce bearing corrosion by neutralizing the corrosive acids. Other inhibitors such as zinc dithiophosphates and phosphosulfurized olefins not only inhibit oxidation but also form a protective film on the bearing surface, making it impervious to acid attack.

Lubricant Properties

Phenolic Inhibitors (Chain-Breaking)
The inhibitor efficiency of phenol is markedly increased by substituting alkyl groups in the two ortho and para positions. It is particularly enhanced when the ortho substituents are bulky groups such as tert-butyl and the para substituent is a primarily alkyl group. A variety of hindered phenols are produced commercially and employed as inhibitors in transformer, turbine, and engine oils.
The methylenebis structure is more effective in high-temperature applications due to its lower volatility characteristics compared to the other molecule.
Zinc Dithiophosphates (Peroxide Destroying)
Of greatest commercial importance in engine lubricants are the zinc dithiophosphates, which not only serve as antioxidants but also provide both antiwear and bearing corrosion protection. The zinc dithiophosphates are made as follows:
Lubricant Properties
where R = alkyl or aryl. Both alkyl and aryl derivatives are employed commercially. Alkyl derivatives are generally more effective as antiwear additives. Aryl derivatives have a higher degree of thermal stability.
Both the antiwear and thermal stability characteristics of the alkyl compounds can be varied by using different alcohols; i.e. primary vs. secondary and high vs. low molecular weight. The principal alkyls are propyl, butyl, hexyl, octyl, and mixtures of these. The effect of the alkyl radical on the thermal decomposition temperature of zinc dialkyldithiophosphates (ZDP) is shown below:
Effect of Alkyl Radical on Thermal Decomposition of ZDP


Alkyl Radical

Decomposition Temperature (°C)

Isopropyl

196

4-Methyl 2-pentyl

197

N-Amyl

212

N-Octyl

>251

Stability increases with the length of the alkyl chain and is lower for secondary alkyl groups with the same number of carbon atoms. It should be noted, however, that the overall performance characteristics of ZDPs are not related to the decomposition temperature.
Antiwear Additives
Wear is the loss of metal with subsequent change in clearance between surfaces moving relative to each other. If continued, it will result in equipment malfunction. Among the principal factors causing wear are metal-to-metal contact, presence of abrasive particulate matter, and attack of corrosive acids.
Metal-to-metal contact can be prevented by adding film-forming compounds that protect the surface either by physical absorption or chemical reaction. The zinc dithiophosphates are widely used for this purpose and are particularly effective in reducing wear in valvetrain mechanisms. These compounds are described under oxidation and bearing corrosion inhibitors. Other effective additives contain phosphorus, sulfur, or combinations of these elements.
Abrasive wear can be prevented by effective removal of particulate matter by filtration of both the air entering the engine and the lubricant during engine operation.
Corrosive wear is largely the result of acidic blowby products formed during fuel combustion. This type of wear can be controlled by using alkaline additives such as basic phenates and sulfonates.
Viscosity Modifiers
Viscosity modifiers, or viscosity index improvers as they were formerly known, comprise a class of materials that improves the viscosity/temperature characteristics of the lubricant. This modification of rheological properties results in increased viscosity at all temperatures. The viscosity increase is more pronounced at high temperatures which significantly improves the viscosity index of the lubricant. This is manifested by a decrease in the slope of the viscosity/temperature line plotted on ASTM log paper.
Lubricant Properties
Viscosity modifiers are generally oil-soluble organic polymers with molecular weights ranging from about 10,000 to 1 million. The polymer molecule in solution is swollen by the lubricant, and the volume of the swollen entity determines the degree to which the polymer increases viscosity. The higher the temperature, the larger the volume and the greater the "thickening" effect of the polymer. Hence, the oil tends to "thin" less due to increased temperature.
In addition to viscosity improvement, the performance of these polymers also depends on shear stability or resistance to mechanical shear and on their chemical and thermal stability. With a given polymer system, shear stability decreases with an increase in molecular weight. The loss due to shear is reflected in a loss in lubricant viscosity. On the other hand, the "thickening power" of the viscosity modifier increases with an increase in molecular weight for a given polymer type. A performance balance must then be established which takes into consideration shear stability and viscosity needs as well as thermal and oxidative stability in actual engine operation.
Pour Point Depressants
Pour point depressants prevent the congelation of oil at low temperature. This phenomenon is associated with crystallization of the paraffin wax that is present in mineral oil fractions. To provide low pour points, the refiner removes wax constituents, which solidify at relatively high temperatures, in a process known as dewaxing. Complete dewaxing would reduce the yield of lube oil to an uneconomical level. Therefore, the dewaxing process is supplemented by using additives that lower the pour point of the oil.
Lubricant Properties
Pour point depressants do not prevent wax from crystallizing in the oil. Rather, they are absorbed on the wax crystals and, thus, reduce the amount of oil occluded on the crystal. Reducing the crystal volume permits lubricant flow.
Miscellaneous Additives
This category includes antirust compounds and foam inhibitors. Chemicals employed as rust inhibitors include sulfonates, alkenyl succinic acids, substituted imidazolines, amines, and amine phosphates. A considerable amount of information on these additives is contained in patent literature. Antifoam agents include silicones and miscellaneous organic copolymers.

Lubrication Theory and Practice
Additive Use

While the general nature of additives may be the same for various types of lubricants, the specific types of additives chosen will depend upon the service in which the lubricant will be used and the characteristics of the base fluid. The development of a balanced additive package involves considerably more work than the casual use of each additive type mentioned. Extensive full-scale testing, both in the laboratory and in the field, is necessary to develop a suitable product.
Quite often, functional difficulties arise under actual operating conditions from combining these materials. On the other hand, unpredictable but desirable synergistic effects may also become evident. The only methods currently available to obtain such data are full-scale tests, some of which will be described below.
As noted previously, the principal functions of a lubricant are contaminant containment, heat removal and friction reduction. The important factors that influence these functions are:
Factors Influencing Lubricant Functions


Contaminant Containment

1. Detergency — Dispersancy
2. Corrosion Prevention
3. Rust Protection
4. Stability — Thermal and Oxidative

Heat Transfer

1. Specific Heat
2. Thermal Conductivity
3. Stability — Thermal and Oxidative

Reduction of Frictional Effects

1. Coefficient of Friction
a. Oiliness or Antiwear
b. Antiweld, Antiseize
2. Viscosity/Temperature Index
3. Pressure/Viscosity Effect
4. Stability — Thermal and Oxidative

Note that thermal and oxidative stability are necessary to perform all functions.
Engine Lubricants
Most engines used in transportation are of the internal combustion type. These engines have high thermal efficiency and are lightweight relative to their power capability. The performance of engine lubricants is judged on their ability to reduce friction, resist oxidation, minimize deposit formation, and prevent corrosion and wear. To meet these functional requirements, engine lubricants must be supplemented with additives, as follows:

  • Antiwear additives
  • Viscosity modifiers
  • Pour point depressants
  • Antifoam agents
  • Friction modifiers
  • Antioxidants
  • Viscosity modifiers
  • Dispersants
  • Detergents
  • Antirust additives
  • Bearing corrosion inhibitors

Most problems associated with engine lubricants are related to lubricant decomposition and the entry of combustion byproducts into the crankcase. The major causes of engine malfunction due to lubricant quality are deposit formation, contamination, oil thickening, oil consumption, ring sticking, corrosion, and wear.
Deposit Formation
The two main sources of lubricant contamination are blow-by from the combustion chamber, and gases and volatiles from the crankcase that are vented into the intake manifold as an antipollution measure. The various gases interact with one another and the lubricant to form soot, carbon, lacquer, varnish, and sludge.
Soot particles are hydrocarbon fragments partially stripped of hydrogen atoms. They also contain an appreciable amount of oxygen and sulfur. Soot particles are strongly attracted to one another and to polar compounds in the oil. Soot tends to form aggregates, which have a soft and flaky texture, and is commonly found in the combustion chamber.
Carbon deposits are hard and result from the carbonization of the liquid lubricating oil and fuel on hot surfaces. These deposits have a lower carbon content than soot and usually contain oily material and ash. They are commonly found on the piston top lands and crowns, in piston ring grooves, and on valve stems.
Lacquer and varnish form when oxygenated products in the lubricant are exposed to high temperatures. Lacquer is often derived from the lubricant and is generally water soluble. It is commonly found on pistons and cylinder walls and in the combustion chamber.
Varnish, on the other hand, is fuel related and is acetone soluble. It is commonly found on valve lifters, piston rings, and positive crankcase ventilation valves.
Sludge is caused by lubricant oxidation, oxidation and combustion products in the blow-by gas, and the accumulation of combustion water and dirt. It can vary in consistency from that of mayonnaise to a baked deposit. Low-temperature sludge, most prevalent in gasoline engines, is watery in appearance and forms below 95°C. High-temperature sludge is more common in diesel engines and forms above 120°C.
Oil Thickening
Oil thickening can result from lubricant oxidation, the accumulation of insolubles, and soot. Viscosity increases due to:

  • Polymerization of oxygenated products
  • Suspension of fuel-derived insolubles in the bulk lubricant

Oil Consumption
Oil consumption is related mainly to the lubricant that travels past piston rings and valves, and burns in the combustion chamber. The extent of lubricant consumption depends on a number of equipment and lubricant related factors, including viscosity, volatility and seal-swell characteristics.
A certain minimum amount of oil is required to properly lubricate the cylinder walls and pistons. High oil consumption, however, indicates a problem such as cylinder wear, bore polishing, stuck piston rings or out of square grooves. These conditions increase the amount of blow-by gases entering the crankcase.
Lubricant volatility is another important factor responsible for oil consumption. Lighter base oils can leak past the piston rings more readily and be burned.
Ring Sticking
The major cause of ring sticking is the formation of deposits in the piston grooves, resulting in the loss of an oil seal. This not only increases the potential for blow-by gases in the crankcase but also leads to poor heat transfer from the piston to the cylinder wall. Resultant thermal expansion of the pistons can lead to loss of compression and engine seizure.
Corrosion and Wear
Diesel fuel with high sulfur content causes piston ring and cylinder wear. Corrosive wear is more commonly associated with combustion and oxidation products; it results from the attack of sulfur acids or organic acids on iron surfaces. This kind of wear is controlled by using lubricants with a base reserve.
Engine Oil Performance
In the U.S., the classification of and requirements for engine oils are established through a process led by API, AAMA, EMA and CMA. These trade associations, together with ILMA, provide the framework for new engine oil categories. The technical societies ASTM and SAE verify the technical need for the new category and ultimately recommend the tests and performance limits to define the category.
In Europe, individual OEMs continue to be a major influence on engine oil performance requirements for both passenger-car and heavy-duty applications. The ACEA classification system consists of nine different sequences to define engine oil quality for European automotive service fill applications. The system is based on a schedule of physical, chemical and engine tests similar to those used in the U.S. but using both ASTM and CEC test methods. All performance claims against ACEA requirements must be supported by data generated under the European Engine Lubricant Quality Management System (EELQMS). This system consists of two codes of practice — one developed by ATC and one by ATIEL — and defines the process for developing, testing and reporting the necessary performance data.
In the U.S., API administers the licensing and certification of engine oils through a system that meets the warranty, maintenance and lubrication requirements of original equipment manufacturers (OEMs). Engine oil performance requirements, test methods, limits for the various classifications and testing processes are established cooperatively by the OEMs, oil marketers, additive companies and testing laboratories. These groups routinely review the classifications system and implement changes as conditions warrant. Click here to view current API Engine Service Classifications for gasoline and heavy-duty diesel engine oils, and the physical requirements for engine oils.
Gasoline Engine Lubrication
Lubrication problems in gasoline engines, particularly in passenger cars, are associated with:

  • Low-temperature or light-duty operation, resulting in excessive contamination of the lubricant by partially burned fuel fragments and other blow-by products.
  • High-temperature oxidation, resulting in excessive engine rust and sludge that can lead, among other things, to excessive oil thickening.
  • Valvetrain wear resulting from the high cam lift and spring loads required to provide high volumetric efficiency and high engine speeds.
  • The use of air-pollution control devices such as positive crankcase ventilation and exhaust gas recirculation.

Recognizing these problems, the automobile industry has sought to define the lubrication requirements of their engines in terms of engine dynamometer test procedures. Some of these test sequences are published by ASTM and involve:

  • Sequence IID — Low-temperature deposits and rusting.
  • Sequence IIIE — Oil thickening and valvetrain wear.
  • Sequence VE — Performance of lubricants under stop-and-go driving conditions.

In North America, all licensed oils must meet the requirements of ILSAC GF-2 and API SJ. The procedures for licensing and certifying engine oils by API are complemented by the Chemical Manufacturers Association (CMA) Product Approval Code of Practice, which provides a statistically valid testing and approval system for testing candidate oils. A key provision of the Code is multiple-test acceptance criteria for the Sequence IID, IIIE, VE, VI-A and L-38 tests.
In Europe, all licensed oils for gasoline powered engines must meet the requirements of ACEA A1, A2, or A3.
Diesel Engine Lubrication
Lubrication requirements for diesel engines are being driven by emission control requirements. New engine designs are being introduced to meet the latest emissions regulations, which are listed below. These changes subject the lubricant to more hostile operating conditions.


Year

CO
(g/bhp-h)

PM
(g/bhp-h)

HC
(g/bhp-h)

NOx
(g/bhp-h)

1994

15.5

0.1

1.3

5.0

1998

15.5

0.1

1.3

4.0

2004 — Option 1

15.5

0.1

*NMHC + NOx =2.4

2004 — Option 2

15.5

0.1

*NMHC + NOx =2.5

*Nonmethane Hydrocarbons cap of 0.5 g/hp-h in Option 2
In reducing emissions, the lubricant has been identified as a direct contributor to hydrocarbon particulates. This occurs partly from the leakage of lubricant past exhaust valve guides and turbocharger seals, but mainly from consumption of the lubricant film on the cylinder liner during combustion. To reduce particulate emissions, new engines are designed to operate with a thinner lubricant film and to allow less lubricant leakage past the piston rings. Unfortunately, this can increase the potential for ring and liner scuffing, and can increase operating temperatures and the potential for deposit formation. In addition, the engine modifications and adjustments necessary to ensure compliance with 1994 exhaust emissions regulations also had the adverse effect of increasing lubricant soot levels, which can increase wear and oil viscosity.
In the U.S., oils intended for use in low-emissions diesel engines must meet the requirements of API CH-4. Deposit control performance of lubricants intended for low-emissions engines is evaluated in the Caterpillar 1P single-cylinder engine test. The Roller-Follower Wear, Mack T-8E and Mack T-9 tests measure a lubricant's ability to guard against serious soot-related problems such as valvetrain wear, viscosity increase and filter plugging.
In addition, lubricants to be used in four-stroke diesel engines operating on high-sulfur fuels must meet the requirements API CF, while lubricants to be used in modern two-stroke diesel engines must meet the requirements API CF-2.
Similar requirements are influencing the development of engine oil requirements in Europe, where ACEA has issued diesel engine oil specifications for both light-duty dieseland commercial vehicles.
U.S. Military
The U.S. military diesel engine oil specification, MIL-PRF-2104G, covers engine oils suitable for lubricating spark and compression ignition internal combustion engines. Engine performance tests used for MIL-PRF-2104G qualification are the Caterpillar 1M-PC and 1N, Mack T-8, Roller Follower Wear and HUEI Oil Aeration Tests.
MIL-PRF-2104G implements API CG-4, CF and CF-2 diesel engine oil requirements. The specification also covers power transmission fluid applications in combat/tactical service by including the transmission test requirements of Allison C-4and Caterpillar TO-4. These requirements cover graphite, paper and bronze friction; friction retention; gear wear testing; and seal compatibility. It should be noted that compliance with the TO-4 test requirements in MIL-PRF-2104G does not constitute full compliance with the Caterpillar specification.
Gear Lubricants
The primary functions of a gear lubricant are the same as those for all lubricants. However, particular emphasis might be placed on friction reduction and heat removal. Contaminant containment, while important, is not as difficult as with crankcase lubricants because no fuel degradation products are present.
The principal types of additives used for gear lubricants are:

  • Antiwear and extreme pressure additives
  • Antifoam agents
  • Antioxidants
  • Antirust additives

The oxidation, rust and foam inhibitors used in gear lubricants are generally of the same type as those used in crankcase lubricants.
Of particular importance are antiwear and extreme pressure additives, which are activated only under specific temperature and pressure conditions and are inactive under other conditions. This property is necessary both to preserve the reagents and to avoid extraneous reactions that might be detrimental to the system. Examples of harmful side effects are excessive wear on gear teeth, ball and roller bearing parts, and other differential components, as well as possible deposits in oil passages and other critical areas.
Combining the necessary additive properties in a single gear lubricant package is not a simple matter. A major stumbling block is the difficulty in reconciling high-speed and high-torque requirements. Some materials that enhance one type of performance can hinder the other. Because of the complexity involved, many full-scale passenger car and truck axle tests must be run, both in the laboratory and on the road. These tests require the support of numerous chemical and physical bench tests to screen out the most promising candidates.
To completely specify a gear lubricant, both the API service designation and SAE viscosity grade are required. Viscosity should be selected based on minimum and maximum service temperatures. Multigrade fluids are normally used, and each viscosity grade has distinct criteria for low and high-temperature performance.
Passenger car rear axle lubricants require score protection as well as thermal and oxidative stability and rust protection. This is provided through the use of sulfur-phosphorus lubricants. Requirements for these lubricants are described in the API GL-5 specification.
The requirements of many equipment builders exceed those of the API specifications. As a result, SAE and ASTM have updated GL categories to reflect present and future needs. This action has promoted the development of gear lubricant categories API MT-1 and proposed PG-2, which are designed to meet the performance requirements of North American heavy-duty or commercial equipment.
API MT-1 designates oils for heavy-duty truck and bus manual transmissions. Its focus is on improved high-temperature cleanliness and stability, oxidation and antiwear control, and compatibility with oil seals and copper alloys.
PG-2 is for heavy-duty truck and bus final drive axles using spiral bevel and hypoid gears. It also includes requirements for improved high-temperature properties and seal compatibility. Tests included in the proposed specification are:
Tests for Proposed Gear Oil Category PG-2


Required Performance

Recommended Test

Thermal Stability/Component Cleanliness

L-60 (Intevep rating procedure)

Oil Seal Compatibility

ASTM D 471

Copper Compatibility

ASTM D 130 (3 h at 121°C)

Gear Surface Fatigue

Mack Spalling

API GL-5 Performance

Current API GL-5 Tests

Compatibility with existing gear lubricants

SS&C FED-STD-791 Method D3430 & 3440


The U.S. Military recently updated its gear oil specification to MIL-PRF-2105E. This specification combines the requirements of 2104D and API MT-1. MIL-PRF-2105E requires heavy-duty manual transmission field testing in addition to the heavy and light-duty axle testing currently required.
Many automobile manufacturers have proprietary test requirements for their factory-fill gear lubricants. As such, factory-fill oils provide unique performance characteristics that are critical for the satisfactory operation of a particular OEM's drivetrain. Their performance characteristics may include break-in, bearing preload and limited-slip durability. However, API GL-5 lubricants are often recommended for service-fill applications.
The quality of European gear oils is influenced primarily by the requirements of the major commercial vehicle and passenger car manufacturers. API GL-5 and MIL-L-2105D establish the minimum performance level for European commercial vehicles. Equipment builders then impose additional requirements to meet their specific needs for improved surface fatigue, component cleanliness, synchromesh durability and viscometrics.
The majority of passenger cars now use a transaxle drivetrain arrangement, reducing the need for rear axle lubricants. These vehicles are filled for life at the factory. Conventional API GL-4 lubricants are being replaced by more specialized manual transmission fluids. These fluids have excellent thermal stability and carefully tailored frictional characteristics to provide smooth synchronization and good shift quality.
A performance area not addressed by industry specifications is limited slip. Because of hardware differences among the various limited-slip differentials, no standard industry-wide test is available to evaluate a lubricant's ability to prevent chatter in this application. Lubricant requirements, therefore, are based on performance in an individual manufacturer's test rig or vehicle.
Automatic Transmission Fluids
The principal functions of automatic transmission fluids (ATFs) are:

  • Power transmission in the fluid member (torque converter)
  • Hydraulic control medium
  • Heat transfer medium
  • Lubrication of transmission parts such as clutches, gears, bearings, and seals
  • Friction modification

The general types of additives used to enhance these functions are: 

  • Antioxidants
  • Dispersants
  • Extreme pressure additives
  • Friction modifiers or "oiliness" agents
  • Pour point depressants
  • Viscosity modifiers
  • Seal conditioners
  • Corrosion inhibitors
  • Antifoam agents

A critical problem in developing an ATF is providing the desired frictional properties for proper clutch pack operation while still providing the other properties. Because of differences in transmission design among the major auto manufacturers, the required frictional properties vary considerably. One design may require a "slippery" fluid with a low coefficient of friction at lock-up to provide a smooth shift without the noise and wear produced by stick/slip. Another might require a higher coefficient of friction to ensure fast clutch plate lock-up that prevents wear due to excessive slippage.
ATFs must also have a sufficiently high viscosity at elevated temperatures to ensure against excessive leakage in hydraulic and control systems. This would result in low hydraulic pressures and degradation of shift characteristics. In addition, too high a viscosity at low temperatures causes reduced fluid flow, which causes reduced fluid efficiency, pump cavitation, extended shift time, possible clutch plate failures, and reduced starting capability.
Modern vehicle and transmission designs place increased stress on the automatic transmission fluid. The drive to improve fuel economy has led to more aerodynamic car designs that permit less airflow around transmission, thereby increasing operating temperatures. This, combined with reduced sump sizes, results in severe thermal stress on the fluid.
Requirements in both the General Motors DEXRON®-III and Ford MERCON® specifications are aimed at avoiding problems caused by high-temperature operation. The 4L60 oxidation test in DEXRON®-III ensures that the fluid keeps transmission parts virtually sludge free. In addition, the specification severely limits total acid number (TAN) increase. Likewise, MERCON® limits maximum viscosity increase in the aluminum beaker oxidation test to 40% to prevent high-temperature oxidation problems.
Automakers are offering longer drivetrain warranties; therefore, increased emphasis has been placed on improved durability and consistent shift quality. Providing the proper friction performance is a vital role for an ATF. The band and plate friction tests, and 4L60 cycling test in DEXRON®-III, and the MERCON® friction durability test ensure that a transmission retains its shift quality throughout the life of a vehicle.
Electronic controls are common in modern transmissions, and the smaller fluid orifices required for these controls challenge an ATF's rheology, especially in cold weather. To ensure proper operation, particularly at start-up, ATFs must have improved low-temperature viscosity. Therefore, both DEXRON®-III and MERCON® require a maximum viscosity of 20,000 cP at -40°C.
Another important property of and ATF is compatibility with elastomer seals. The fluids can affect the tensile strength, elongation, hardness and volume of elastomers. Various immersion tests are generally used to evaluate the compatibility of ATFs with the different seal materials.
Several other fluid properties are important for the proper functioning of an automatic transmission, including lubrication of the moving parts, foam resistance, low volatility, low pour point, and high flash and fire points. Generally, the technology required to provide these properties is not as complicated as that to produce the other properties discussed.

 

 

 

Source: http://www.todaystrucking.com/images/Lubrication_Theory_and_Practice4.doc

Web site to visit: http://www.todaystrucking.com

Author of the text: indicated on the source document of the above text

If you are the author of the text above and you not agree to share your knowledge for teaching, research, scholarship (for fair use as indicated in the United States copyrigh low) please send us an e-mail and we will remove your text quickly. Fair use is a limitation and exception to the exclusive right granted by copyright law to the author of a creative work. In United States copyright law, fair use is a doctrine that permits limited use of copyrighted material without acquiring permission from the rights holders. Examples of fair use include commentary, search engines, criticism, news reporting, research, teaching, library archiving and scholarship. It provides for the legal, unlicensed citation or incorporation of copyrighted material in another author's work under a four-factor balancing test. (source: http://en.wikipedia.org/wiki/Fair_use)

The information of medicine and health contained in the site are of a general nature and purpose which is purely informative and for this reason may not replace in any case, the council of a doctor or a qualified entity legally to the profession.

 

Lubrication Theory and Practice

 

The texts are the property of their respective authors and we thank them for giving us the opportunity to share for free to students, teachers and users of the Web their texts will used only for illustrative educational and scientific purposes only.

All the information in our site are given for nonprofit educational purposes

 

Lubrication Theory and Practice

 

 

Topics and Home
Contacts
Term of use, cookies e privacy

 

Lubrication Theory and Practice