Overview of Asphalt Emulsion

asphalt emulsion

The use of asphalt emulsions began in the early part of the 20th century. Today 5% to 10% of paving-grade asphalt is used in emulsified form, but the extent of emulsion usage varies widely between countries. The United States is the world’s largest producer of asphalt emulsion.

The advantages of asphalt emulsion compared to hot asphalt and cut back binders are related to the low application temperature, compatibility with other water-based binders like rubber latex and cement, and low-solvent content.

The paper gives an introduction to the chemistry of asphalt emulsion. The role of the emulsion components—asphalt, emulsifiers, acids or alkalis, and additives—in determining the physical properties and reactivity of the emulsion is described. Recent advances in the understanding of the setting process are outlined. The classification of emulsions into grades according to their reactivity, particle charge, and physical properties is explained and typical recipes of various emulsion grades are given. The selection of the correct emulsion grade for the various applications based on emulsion reactivity and physical properties of the emulsion is covered in general terms.

The past 20 years have seen considerable progress in the understanding of how emulsion chemistry influences performance. Consequently formulations can be developed to optimize the performance of the construction material or construction process rather than simply to meet

standard specifications. The result has been faster-setting surface treatments, quick-drying tack coats, penetrating emulsion primes that are superior to cut backs, and cold-mixed materials with improved properties.

USE OF ASPHALT EMULSION

The first asphalt (bitumen) emulsions used in road construction were prepared in the early part of the 20th century. Today approximately 3 million tons of emulsions are produced in the United States representing about 5% to 10% of asphalt consumption. More than 8 million tons of emulsions are produced worldwide. Emulsion production varies greatly among countries with the United States, France, Mexico, and Brazil being significant producers (1).

ADVANTAGES OF EMULSION

With viscosities in the range 0.5–10 Poise at 60°C, asphalt emulsion is of considerably lower viscosity than asphalt itself (100–4,000 Poise), allowing it to be used at lower temperature. Lowtemperature techniques for construction and maintenance reduce emissions, reduce energy consumption, avoid oxidation of the asphalt, and are less hazardous than techniques using hot asphalt. They are also more economical and environmentally friendly than cold techniques using cut back asphalts. The environmental benefit of asphalt emulsion is particularly positive when used for in-place or on-site techniques which avoid the energy usage and emissions associated with heating, drying, and haulage of aggregate. The construction of a roadway with cold techniques has been calculated to consume approximately half the energy of one of similar bearing capacity made with hot-mix asphalt (HMA) (2). An environmental impact analysis (EIA) technique called “eco-efficiency” has been applied to emulsion maintenance techniques (microsurfacing and chip seal) and it was concluded that the emulsion system had less environmental impact than a thin hot-mix overlay (3).

Emulsions are water-based and in many cases can be diluted further with water for applications such as dust control and priming. They are also compatible with hydraulic binders like cement and lime as well as water-based polymer dispersions like natural and synthetic latex.

When mixtures of cement, latex, and asphalt emulsion cure, a composite binder is produced with a structure that cannot be duplicated with hot asphalt and with significantly improved properties compared to pure asphalt (4,5).

EMULSION DEFINITION

An emulsion is a dispersion of small droplets of one liquid in another liquid. Typical examples include such everyday products as milk, butter, mayonnaise, and cosmetic creams. Emulsions can be formed by any two immiscible liquids, but in most emulsions one of the phases is water.

Oil-in-water (O/W) emulsions are those in which the continuous phase is water and the disperse (droplet) phase is an “oily” liquid. Water-in-oil (W/O) “inverted” emulsions are those in which the continuous phase is an oil and the disperse phase is water. Emulsions can have more complex structures. In multiple emulsions, the disperse phase contains another phase which may not have the same composition as the continuous phase (Figure 1). Types of emulsions

Standard bitumen (asphalt) emulsions are normally considered to be of the O/W type and contain from 40% to 75% bitumen, 0.1% to 2.5% emulsifier, 25% to 60% water plus some minor components which are described below. The bitumen droplets range from 0.1–20 micron in diameter. Emulsions with particle sizes in this range are sometimes referred to as macroemulsions.

They are brown liquids with consistencies from that of milk to double cream, which depend mostly on the bitumen content and the particle size. Some bitumen droplets may contain smaller water droplets within them; a better description of asphalt emulsion would be a W/O/W multiple emulsion. The viscosity of the emulsion and especially changes in the viscosity of the emulsion during storage are strongly influenced by this internal water phase (6,7).

There is a distribution of particle sizes in the emulsion, and this distribution is influenced by the emulsion recipe and the mechanics and operating conditions of the emulsion manufacturing plant (Figure 2). The particle size and the particle size distribution of the emulsion droplets strongly influence the physical properties of the emulsion, such as viscosity and storage stability; larger average particle size leads to lower emulsion viscosity, as does a broad or bimodal particle size distribution (8). Particle size also influences the performance of emulsion. In general, smaller particle size leads to improved performance in both mix and spray applications (9). Some recent developments in asphalt emulsion technology have focused on the ability to control the particle size and size distribution of the emulsion during the emulsification process, and consequently to influence the emulsion properties (10–12).

Macroemulsions are inherently unstable. Over a period of time, which may be hours or years, the asphalt phase will eventually separate from the water. Asphalt is insoluble in water, and breakdown of the emulsion involves the fusion of droplets (coalescence) (Figure 3).

The asphalt droplets in the emulsion have a small charge. The source of the charge is the emulsifier, as well as ionisable components in the asphalt itself. These small charges on the droplets normally provide an electrostatic barrier to their close approach to each other (like charges repel). However, when two droplets do achieve enough energy to overcome this barrier and approach closely then they adhere to each other (flocculate). This flocculation may sometimes be reversed by agitation, dilution, or addition of more emulsifier. Over a period of time the water layer between droplets in a floccule will thin and the droplets will coalesce. The coalescence cannot be reversed. Factors which force the droplets together such as settlement under gravity, evaporation of the water, shear or freezing will accelerate the flocculation and coalescence process, as does anything which reduces the charge on the droplets. Lower viscosity asphalts coalesce more rapidly than high viscosity asphalts. Of course, eventually we want the emulsion droplets to coalesce after the asphalt emulsion has come in contact with the aggregate and been placed on the roadway. Setting and curing of emulsion are discussed in more detail below.

Typical particle size distributions of asphalt emulsions

Stages in the breakdown of emulsions

CLASSIFICATION AND NAMING OF EMULSIONS

Bitumen emulsions are classified according to the sign of the charge on the droplets and according to their reactivity. Cationic emulsions have droplets which carry a positive charge.

Anionic emulsions have negatively charged droplets. Rapid-setting (RS) emulsions set quickly in contact with clean aggregates of low-surface area, such as the chippings used in chip seals (surface dressings). Medium-setting (MS) emulsions set sufficiently less quickly that they can be mixed with aggregates of low surface area, such as those used in open-graded mixes. Slowsetting (SS) emulsions will mix with reactive aggregates of high surface area. RS emulsions are reactive and are used with unreactive aggregates; SS emulsions are unreactive and are used with reactive aggregates. The actual setting and curing time in the field will depend on the technique and materials being used as well as the environmental conditions.

In the naming of emulsions according to ASTM D977 and D2397, cationic RS, cationic MS, and cationic SS emulsions are denoted by the codes CRS, CMS, and CSS, whereas anionic emulsions are called RS, MS, and SS, followed by numbers and text indicating the emulsion viscosity and residue properties. For example SS-1H would be a slow-setting (i.e., low reactivity) anionic emulsion with low viscosity and a hard asphalt residue. CRS-2 would be a reactive cationic emulsion of high viscosity. The QS (quick-setting) and CQS (cationic quicksetting) designations for quick-setting emulsions have been introduced for emulsions intermediate in reactivity between MS and SS, which do not need to pass the cement mix test, and are used primarily in quick-set slurry surfacing applications.

Local authorities have many other naming schemes associated with emulsions with particular properties. In state department of transportation (DOT) specifications letters such as P or LM may indicate polymer-modified or latex-modified asphalt emulsion, S may indicate high solvent content, and terms such as AEP (asphalt emulsion prime) and PEP (penetrating emulsion prime), and ERA (recycling agent emulsion) may indicate emulsions with specific uses.

TESTING EMULSION

Emulsion testing will be addressed in detail in another paper. Most test methods have been accepted as ASTM standards. The tests fall into three groups: those that test the handling properties of the emulsion, such as residue content, viscosity, and storage stability sieve residue; those that classify the emulsion into rapid-, medium-, or slow-setting grades, such as demulsibility, cement mix test, and coating tests; and tests on the residue recovered by evaporation, such as penetration or ductility. The emulsion may then be subject to additional performance tests related to the particular application of the emulsion in cold mix, chip seal, etc., using job aggregates.

EMULSION APPLICATIONS

Applications will be addressed in detail in other papers. Some typical applications of the various grades of emulsion are summarized in Table 1, but local practice varies considerably. The choice of emulsion for each application is a question of matching the reactivity of the emulsion with the reactivity of the aggregate and the environmental conditions. Aggregate reactivity is mostly associated with the very finest-size fractions which make the highest contribution to surface area.

So a reactive RS emulsion is used with the low-surface area unreactive aggregates used in chip seal, whereas a low-reactive SS emulsion would be used for a dense cold mix which has a high content of –75 micron material and consequently high reactivity.

Environmental conditions also have to be taken into account. High temperatures accelerate the chemical reactions and physical processes involved in emulsion setting, and therefore demand slower setting emulsions.

MANUFACTURE OF EMULSION

Emulsions are made by mixing hot bitumen with water containing emulsifying agents and applying mechanical energy sufficient to break up the bitumen into droplets. The effect of manufacturing variables on emulsion properties will be described in detail in a later paper.

It is clear that the manufacturing process can not only affect the physical properties of the emulsion but also affects the performance of the emulsion.

Emulsification is opposed by the internal cohesion and viscosity of the bitumen and the surface tension of the droplet which resists the creation of new interface. Smaller droplets are favored by a high energy input, a low bitumen viscosity at the emulsification temperature and by the choice and concentration of emulsifier (which reduces the interfacial tension). In the most common process, the emulsifier is dissolved in the water phase of the emulsion, and this water solution or “soap” is mixed with the hot liquid asphalt in a colloid mill (Figure 4).

Typical Uses of Emulsion

CHEMICAL NATURE OF EMULSIFIERS

Water molecules at the interface between oil and water have higher energy than those in bulk water. The result is an interfacial energy or tension which acts to minimize the interfacial area.

The production of emulsion involves the creation of a large interfacial area between the asphalt and water, approximately 500 m2 per liter (10). Emulsifiers are surface active agents (surfactants).

Batch emulsion plant

Surfactants have nonpolar lipophilic (oil-loving) and polar hydrophilic (water-loving) portions in the same molecule (Figure 5). The molecules concentrate at the interface between water and bitumen, orientated with the polar group in the water and the nonpolar parts of the molecule in the oil (Figure 6). This both reduces the energy required to emulsify the asphalt and prevents coalescence of the droplets once formed. The choice and concentration of emulsifier also largely determines the charge on the asphalt droplet and the reactivity of the emulsion produced.

A typical emulsifier has a hydrophilic “head” group and lipophilic (hydrophobic) hydrocarbon “tail” comprising 12 to 18 carbon atoms. This hydrocarbon tail is represented by “R” in chemical formulas. It is most often derived from natural fats and oils, tall oil, wood resins, or lignin.

Emulsifiers can be classified into anionic, cationic, and nonionic types depending on the charge their head groups adopt in water, although this charge may depend on pH (Table 2).

Cationic emulsifiers are ammonium compounds contain positively charged nitrogen (N) atoms in their head group; anionic emulsifiers typically contain negatively charged oxygen (O) atoms.

The charge on the head group is balanced by a counterion. The charge on the emulsifier head group largely determines the charge on the asphalt droplets, since the counterion diffuses away from the asphalt surface (Figure 6). Several studies have shown that even nonionic emulsifiers produce emulsions whose droplets have a small negative charge in water (14), and nonionic emulsifiers are often used in slow-setting asphalt emulsions. In the case of asphalt emulsions, the asphalt itself contains surface active species which can also concentrate at the interface (15). The size and sign of the charge on the asphalt droplets can be measured and is expressed as the “zeta potential” of the droplet. The zeta potential is strongly pH-dependent both because of the pH dependence of the charge on the emulsifier and also because polar components of the asphalt itself may ionize. Zeta potential measurements show that the charge on the asphalt droplets becomes more negative as the pH rises.

As the concentration of the emulsifier increases, the particle size of the emulsion is reduced. SS emulsions, which contain higher concentrations of emulsifier, generally have smaller particle size than RS grades.

Cationic emulsifier molecule

Origin of charge on asphalt droplets

Chemistry of Asphalt Emulsifiers

Generally more emulsifier is required to provide good stability and the right performance properties to the emulsion than is necessary to fill the interface, so asphalt emulsions will contain some “free” emulsifier in the water phase, present partly in micellar form, which acts as a reservoir helping to prevent coalescence after emulsification and storage and transport. This free emulsifier plays an important role in the setting process (see below) (10, 11). During storage of asphalt emulsion after production there may be slow changes due to migration of polar asphalt components and adsorption of emulsifier from the water phase into the interface (16). This reduces the free emulsifier concentration in the water phase and can influence the emulsion properties.

FORMULATION OF THE EMULSION

Emulsifiers are often supplied in a water-insoluble form to the emulsion producer and need to be neutralized with acid or alkali by the emulsion manufacturer to generate the anionic or cationic water-soluble form used to prepare the soap solution. The choice of the acid or alkali and the final pH of the emulsion influence the emulsion properties. Hydrochloric acid and occasionally phosphoric acid are the acids used, and sodium and potassium hydroxide are the most common alkalis. Cationic emulsions are usually acid, and anionic emulsions are typically alkaline (Table 3).

equation

Some emulsifier types, like quaternary ammonium compounds and alkylbenzenesulphonates, have permanent head group charges and do not need to be reacted with acids or alkalis (Table 2).

These products, as well as nonionic emulsifiers, allow the formulation of emulsions which are neutral in pH.

Increasing emulsifier concentration decreases the reactivity of the emulsion. MS emulsions are generally formulated with the same emulsifiers as RS grades but at higher concentration (0.4%–0.8%). The emulsion producer can adapt the emulsion recipe to cope with reactive aggregates or high temperatures, generally by increasing the emulsifier concentration or blending emulsifiers of lower reactivity.

A wide range of chemistries have been used for asphalt emulsifiers. In addition to cationic, nonionic, and anionic emulsifiers, there are products with amphoteric head group character which may adopt positive or negative charges depending on pH.

OTHER COMPONENTS AND THEIR FUNCTION

Calcium and Sodium Chlorides

Asphalt contains a small amount of salt, which can lead to an osmotic swelling of the droplets in an emulsion as water is drawn into the droplet. This results in an increase in emulsion viscosity, often followed by a decrease as the salt slowly escapes. Calcium chloride or sodium chloride is included in the emulsion at 0.1%–0.2% to reduce the osmosis of water into the bitumen and minimize the changes in viscosity. Sodium chloride is used in anionic emulsions (6).

Adhesion Promoters

Water resistance is an important property of asphalt mixes and seals. The cured film from some anionic emulsions and occasionally also cationic emulsions may not have sufficient adhesion to aggregates, in which case adhesion promoters can be added to the asphalt or to the finished emulsion. Generally these adhesion promoters are surface active amine compounds.

Solvent

Solvents may be included in the emulsion to improve emulsification, to reduce settlement, improve curing rate at low temperatures, or to provide the right binder viscosity after curing. The maximum amount of distillate in the emulsion is usually specified. MS emulsions often contain up to 15% solvent to provide the right workability characteristics and stockpile life to asphalt mixtures. Emulsions used in recycling may also contain solvents and fluxes in order to rejuvenate old asphalt.

Latex

Polymer modification can improve the properties of bitumen in terms of cohesion, resistance to cracking at low temperatures, and resistance to flow at high temperatures. Latex is a water-based dispersion of polymer which is particularly suited to the modification of emulsions. Latex comes in anionic, nonionic, and cationic forms, and it is important that the latex type should be compatible with the emulsion. Styrene butadiene rubber, polychloroprene, and natural rubber latex are most commonly used in paving grade emulsions.

THE SETTING PROCESS

Emulsified asphalt must revert to a continuous asphalt film in order to act as cement in road materials. This involves flocculation and coalescence of the droplets and removal of the water (Figure 3). Evaporation and absorption of water by the aggregate may be the main breaking mechanism for very slow-setting emulsions, but in most cases chemical reactions between the aggregate and the emulsion contribute to the emulsion setting and it is not necessary for all the water to evaporate before curing takes place. The strength of the reaction of emulsion with aggregate is in many cases sufficient to squeeze the water from the system. Clean water can be seen separating from the mixture. The speed of these setting and curing processes depends on the reactivity of the emulsion, the reactivity of the aggregate and environmental factors, such as temperature, humidity, wind speed, and mechanical action. Less viscous asphalts tend to give faster coalescence. It may take a few hours in the case of a chip seal to several weeks in the case of a dense cold mix for the full strength of the road material to be reached.

A considerable amount of research effort, partly sponsored by the European community, has been expended to elucidate the mechanism of setting and curing of asphalt emulsion (17–19).

Important factors are changes in pH caused by reaction of the aggregate with acids in the emulsion, adsorption of free emulsifier onto the aggregate surface, and flocculation of the emulsion droplets with the fines. The relative timescale of flocculation (setting) and coalescence (curing) depends on the system, but in general flocculation is the more rapid process in which some water can be expelled from the system and some cohesive strength develops, followed by a slower coalescence process which results in a continuous asphalt phase. This asphalt phase must also adhere to the aggregate.

Coalescence is an inversion process; the O/W emulsion is transformed into a W/O type which then slowly loses its internal water phase. This inversion process is favored as the ratio of asphalt to water in the system increases. The tendency for an emulsion to invert can be determined in laboratory tests and has been related to curing behavior in the field (21).

Aggregates take up a characteristic surface charge in water which depends on the nature of the minerals, the pH, and the presence of soluble salts. So-called “acid” aggregates high in silica tend to take up a negative charge.

Some aggregates, like carbonates, and fillers, like cement, may neutralize acid in cationic emulsions causing the pH to rise and the emulsion to be destabilized. Anionic emulsions may be destabilized by soluble multivalent ions. We can consider two extreme cases of emulsion breaking (17). In the case where the charge on the emulsion droplets is quickly destroyed by pH changes, for example, then the emulsion very quickly flocculates and coalescence begins to occur at a slower rate. This rate is dependent on the viscosity of the binder, as well as environmental conditions; coalescence is slower with high viscosity asphalts and lower temperatures. At the other extreme where the emulsion droplets remain charged, loss of water, either by evaporation or by absorption of water into porous aggregate, eventually forces the droplets close enough for attractive forces to predominate, forcing out water and starting the coalescence process. The attractive forces between the droplets can generate significant cohesion even before coalescence occurs.

In a simplified process (Figure 7) of the setting of a RS cationic emulsion where the aggregate does not contain significant fines, important stages in the setting process can be considered as follows:

Possible stages in the setting of a cationic emulsion

1. Free emulsifier adsorbs onto the (oppositely charged) mineral surface, which
neutralizes some charge on the surface while at the same time making the surface somewhat lipophilic. Too high a free emulsifier concentration in relation to the surface area of the aggregate can actually reverse the charge on the minerals and so inhibit the setting of the emulsion.

2. Minerals neutralize acids in the emulsion, causing loss of charge on the emulsion droplets, leading first to flocculation of the asphalt droplets and then to a slower coalescence of the droplets.

3. Water is adsorbed by the mineral, as well as evaporates from the system.

4. Droplets in contact with the mineral spread on the surface, especially that surface made lipophilic by adsorbed emulsifier, eventually displacing the water film on the aggregate surface.

In the breaking of SS grades, where the aggregate contain high content of fines, heteroflocculation of the droplets of asphalt and the oppositely charged fines may occur, which is sufficiently strong to squeeze out water and form an asphalt mastic. A similar situation is achieved in microsurfacing where filler is intentionally added to initiate setting. Mechanical action, such as compaction or traffic, may squeeze the droplets together, promoting coalescence and squeezing water out of the coalesced film. In practical situations too early coalescence of the asphalt droplets can hinder final curing
by skin formation (20, 21) reducing the evaporation of water. Coalescence throughout the asphalt emulsion film, before water is trapped in the system, is promoted by smaller asphalt droplets with narrow size distribution. Too early coalescence of asphalt droplets in some systems can interfere with the formation of a composite binder formed from latex and asphalt, which depends on latex curing before asphalt (4).

RECENT DEVELOPMENTS

Emulsion Manufacture

The factors influencing the properties of the emulsion are better understood today. The particle size of the emulsion and the free emulsifier concentration can be determined by the manufacturing conditions and viscosity can also be controlled. High residue (>75%) emulsions can be prepared by the production of bimodal particle size distributions (22).

Production of emulsion by static mixer technology (SMEP = static mixer emulsion process) is fully commercialized and holds the possibility of adjusting the particle size distribution of the emulsion and so controlling physical and performance properties of the emulsion (23).

Emulsion Chemistry

In the area of emulsifier chemistry there continues to be innovation, especially in emulsifiers for SS emulsions. The use of phosphoric acid instead of hydrochloric acid in emulsions for microsurfacing and cold mix has been established in Europe, Asia, and recently also in the

Americas. The phosphoric acid system allows a wider range of asphalts to be used (24).

Setting Process

As mentioned above there has been a tremendous improvement in our understanding of the setting process of asphalt emulsion. Some innovative techniques related to the setting process have included the use of breaking agents in cold mix and spray applications (25, 26) to provide accelerated curing; the use of wetting agents as compaction aids in cold mix (27) to allow quicker removal of water and hence earlier bonding of the coalesced asphalt with the mineral surface; cement-free slurry seal systems in which reactive filler is generated chemically in the slurry (28); and emulsions of mixed hard and soft binders for cold mix applications which allow some control over the coalescence process (29). In some novel processes SS and RS emulsions are used in combination in order to provide the right coating and curing behavior.

Applications

The last 20 years have seen several emulsion-based new technologies for road construction and repair, as well as significant improvements over previous emulsion systems. These include ultrathin hot-mix friction courses with modified emulsion bond coat (30); DRM (spray-applied crack seal with emulsion seal surfacing); P.A.S.S. (scrub seal with modified emulsified binder) (31); glass fiber-reinforced chip seal (32); trackless tack coats (26, 33); WAM (warm mix using emulsion or foamed asphalt) (34); and improved chip seal systems (35). Several new systems for cold mix have also been commercialized.

FUTURE DEVELOPMENTS

With the high cost of petroleum-derived materials and environmental pressures on HMAs, the future of asphalt emulsion will be in thin performance-based overlays and seals that use less asphalt, replacing cutbacks in priming applications, reducing the mixing and paving temperatures of asphalt mixes, and general stepwise improvements in current applications to provide more reliable, longer-lasting treatments. There is also the potential to develop more cost-effective materials, particularly when the use of emulsion can create structures and microstructures not easily duplicated by hot techniques.

REFERENCES

1. Symposium of World Road Bitumen Emulsion Producers, Lyon, France. SFERB, Paris, September 2002, p. 59.

2. Kennedy, J. Alternative Materials and Techniques for Road Pavement Construction. DOE Energy Efficiency Office, London, 1997.

3. Takamura, K., K. P. Lok, and R. Wittinger. Microsurfacing for Preventive Maintenance: Eco-Efficient Strategy. Proc., 39th ISSA Annual Meeting, Maui, Hawaii, March 2001.

4. Takamura, K. Forced Air Drying and Superpave Analysis of Emulsion Residue. Proc., ISSA 39th Annual Meeting, Maui, Hawaii, March 2001.

5. Brown, S. F., and D. Needham. A Study of Cement Modified Bitumen Emulsion Mixtures. Proc., Annual Meeting of the Association of Asphalt Paving Technologists, 2000.

6. Furlong, S., A. James, E. Kalinowski, and M. Thompson. Water Enclosed Within the Droplets of Bitumen Emulsions and Its Relation to Viscosity Changes During Storage. Colloids and Surfaces (A), Vol. 152, 1999, pp. 147–153.

7. Poirier, J. E., G. Durand, B. Koenders, and M. F. Morizur. Maitrise de la Viscosite des Emulsions de Bitume: La Granulometrie ne peut seule tout expliquer. Proc., 2nd Eurasphalt & Eurobitume Congress(CD-ROM), Barcelona, Spain, 2000.

8. Holleran, G., R. G. Hicks, J. R. Reed. Emulsion Particle Size and Particle Size Distribution Effects in Microsurfacing Emulsion Performance. Paper 4F-044, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

9. Deneuvillers, C., and J. Samanos. Relationship between Characteristics and Properties of Cationic Bitumen Emulsions. Proc., 1st International Symposium on Asphalt Emulsion Technology, Washington, D.C., Nov. 11–14, 1999, pp. 104–112.

10. Boussad, N., and T. Martin. Emulsifier Content in Water Phase and Particle Size Distribution : Two Key Parameters for the Management of Bituminous Emulsion Performance. Paper 6/159, Proc., 1st Eurasphalt and Eurobitume Congress (CD-ROM), 1996.

11. Verlhac, P., F. Verzaro, F. Leal Calderon., J. J. Potti, and B. Eckmann. Characterisation of Bituminous Emulsions: Particle Size Distribution and Amount of Residual Emulsifier. Paper 1C-172, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

12. Poirier, J. E., and G. Durand. Manufacturing Process and Emulsion Properties. Proc., AEMA 21st Annual Meeting, Florida, 1994.

13. Engman, M., A. James, D. Needham., and T. Ng. Specifying Slurry Surfacing Emulsion Quality: Particle Size and Size Distribution. Proc., ISSA 36th Annual Meeting, San Diego, Calif., 1998.

14. Wates, J., and A. James. Zeta Potential Measurements of Bitumen Emulsions and Road Aggregates. Paper 1-40/089, Proc., 1st World Congress on Emulsions, Paris, 1993.

15. Rabiot, D., B. G. Koenders, and M. Andre. A Quality Concept for Emulsion Grade Bitumens. Proc., 1st International Symposium on Asphalt Emulsion Technology, Washington, November 1999.

16. Rodríguez-Valverde, M. Á., M. Á. Cabrerizo-Vílchez, A. Páez-Dueñas, and R. Hidalgo-Álvarez. Kinetic Model of Bitumen Emulsion Breaking. Paper 3C-191, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

17. Lesueur, D., and J. J. Potti. Cold Mix Design: A Rational Approach Based on the Current Understanding of the Breaking of Bituminous Emulsions. Paper 199, Proc., 3rd Eurasphalt and Eurobitume Congress, Vienna, Austria, 2004.

18. Deneuvillers, C. Surfactants, Minerals and Bitumen Interactions: Understanding the Breaking Mechanism of Bitumen Emulsions. Paper 3C-267, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

19. Lesueur, D. Emulsion/Aggregate Interactions through Water Analysis. Paper 0153, Proc., 2nd Eurasphalt and Eurobitume Congress, Barcelona, Spain, 2000.

20. Lesueur, D., C. Coupé, and M. Ezzarougui. Skin Formation During the Drying of a Bitumen Emulsion. Proc., Symposium of World Road Bitumen Emulsion Producers, Lyon, France, 2002, SFERB, Paris, p. 59.

21. Walter, J., and D. Day. Coalescence of Quick Set Surface Dressing PMB Emulsions. Paper 4F-011, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

22. Remtulla, A., and I. Swanston. High Residue Bitumen and Polymer-Modified Bitumen Emulsions for Spray Sealing. Proc., 1st International Conference World of Asphalt Pavements (CD-ROM), AAPA, Sydney, Australia, 2000.

23. Marchal, J.–L. The Esso SMEP Process. Paper 1-12-208, Proc., 1st World Congress on Emulsions, Paris, France, 1993.

24. James, A., and T. Ng. Phosphoric Acid In Microsurfacing Emulsions. To be presented at 13th Congreso Ibero-Latinoamericano del Asfalto (CILA), Costa Rica, 2005.

25. Chaignon, F. A New Concept in Tack Coat Emulsions. Proc., Ist International Symposium on Asphalt Emulsion Technology, Washington, D.C., October 1996, pp. 141–147.

26. Redelius, P. A Novel System for Delayed Breaking Control of Bitumen Emulsions. Paper 1-22-147, Proc., 1st World Congress on Emulsions, Paris, France, 1993.

27. Barreto, G. Compacting Additives in Cold Bitumen Techniques. Plenary Lecture Theme 4-03, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

28. Takamura, K. Portland Cement-Free Microsurfacing. Paper IV/33, Proc., ISSA, Berlin, Germany, 2002.

29. French Patent 2695664, CECA S.A.

30. Serfass, J. P., P. Bense, J. Bonnot, and J. Samanos. New Type of Ultrathin Friction Course. In Transportation Research Record 1304, TRB, National Research Council, Washington, D.C., 1991, pp. 66–74.

31. http://www.westernemulsions.com/pass

32. Chaignon, F. Fibers in Sandwich: An Anticracking Process. Proc., 1st International Symposium on Asphalt Emulsion Technology, Washington, D.C., October 1996, pp. 189–194.

33. Bardesi, O.-E., and D. A. Paez. A Novel Generation of Tack Coat Emulsions to Avoid Adhesion toTyres. Paper 4F-086, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

34. Koenders, B. G., D. A. Stoker, C. Bowen, P. de Groot, O. Larsen, D. Hardy, and K. P. Wilms. Innovative Process in Asphalt Production and Application to Obtain Lower Operating Temperatures. Paper 0088, Proc., 2nd Eurasphalt and Eurobitume Congress, Barcelona, Spain, 2000.

35. Barnat, J. Macro-surfacing: An Innovative Emulsion Chemistry Surface Treatment.  Paper 4F-179, Proc., 3rd World Congress on Emulsions, Lyon, France, 2002.

ALAN JAMES

обновлено: July 4, 2016 автором: dannik