Warm Mix Asphalt (WMA) Additives and Technologies
Warm Mix Asphalt (WMA) technologies reduce HMA production and placement temperatures by 20-40°C through additives or processes: organic waxes (Sasobit), chemica...
Warm Mix Asphalt (WMA) additives enable asphalt production and compaction at temperatures 20-40°C lower than conventional Hot Mix Asphalt (HMA). WMA technologies fall into three categories: organic additives (waxes that reduce binder viscosity), chemical additives (surfactants that improve aggregate coating), and foaming technologies (water injection or zeolites that create temporary binder expansion). Additional benefits include reduced fuel consumption, lower greenhouse gas and fume emissions, improved worker conditions, extended paving season, reduced binder aging, and compatibility with high Reclaimed Asphalt Pavement (RAP) content.
A Warm Mix Asphalt (WMA) additive is a material or technological process that enables the production, placement, and compaction of asphalt mixtures at temperatures significantly lower than conventional Hot Mix Asphalt (HMA). WMA technologies reduce mixing and compaction temperatures by 20–40°C (36–72°F) compared to HMA, which is typically produced at 150–190°C (300–375°F). WMA operates in the temperature range of approximately 100–150°C (212–302°F) , placing it between half-warm asphalt (70–100°C) and conventional HMA on the asphalt production temperature spectrum.

The first WMA techniques were developed in the late 1990s in Europe. The WAM-Foam® process (Warm Asphalt Mix Foam) was developed in Norway through a joint venture between Shell International Petroleum Company and Kolo-Veidekke, while organic wax additives were being trialled in Germany. The motivation for WMA development stems from the 1997 Kyoto Treaty, which set greenhouse gas reduction targets for European countries, prompting the asphalt industry to seek lower-emission production methods. Since the early 2000s, WMA technology adoption has expanded globally, driven by environmental regulations, energy costs, and worker health and safety considerations.
The fundamental challenge that WMA additives address is the need for sufficient binder workability to achieve complete aggregate coating and adequate compaction density at reduced temperatures. In HMA production, high temperatures (150–190°C) reduce the asphalt binder’s viscosity sufficiently to coat aggregates and provide workability during laydown and compaction. Lowering the temperature without an additive would result in high binder viscosity, poor coating, inadequate compaction, and ultimately a pavement with high air voids, reduced durability, and premature failure. WMA additives overcome this barrier through three distinct mechanisms: viscosity reduction (organic waxes), interfacial friction reduction (chemical surfactants), and temporary binder expansion (foaming).
The core concept of WMA is straightforward: produce asphalt mixtures with properties and performance equivalent to HMA while using significantly less energy to heat aggregates and binder. The immediate benefit is a reduction in energy consumption at the asphalt plant — burning less fuel to heat aggregates directly reduces operating costs and emissions. FHWA research indicates that WMA can reduce fuel energy consumption by 3–12% compared to HMA, with some specific technologies achieving up to 30–55% reduction depending on the baseline temperature and technology used.
The environmental and health benefits of WMA are substantial and well-documented. WMA reduces greenhouse gas emissions (primarily CO₂) by 20–35% compared to HMA applications, with 92–96% of total CO₂ reductions attributed to lower fuel consumption at the plant. Emissions of SO₂, NOx, particulate matter (PM10), and volatile organic compounds (VOCs) are all significantly reduced. For worker health, fume (bitumen vapor) emissions are reduced by approximately 50% for every 12°C reduction in temperature — meaning a 30°C temperature reduction yields roughly 80–85% less fume exposure. This creates a cooler, safer working environment for paving crews and reduces odor and emissions for nearby communities and workers in confined areas such as tunnels and parking garages.

WMA offers significant manufacturing and paving benefits beyond emissions reduction. The lower production temperature causes less hardening (aging) of the binder during manufacture, which improves the thermal and fatigue cracking resistance of the pavement over its service life. WMA is fully compatible with Reclaimed Asphalt Pavement (RAP) — in fact, WMA’s lower temperatures allow higher RAP content by reducing additional binder aging that occurs at HMA temperatures. The extended workability of WMA at reduced temperatures enables longer haul distances, extended paving seasons into cooler months, and night paving operations. The same WMA mix produced at HMA temperatures provides a longer compaction window due to the presence of additives, allowing crews more time to achieve target density. Conversely, WMA compacted at its normal lower temperature cools faster to ambient temperature, allowing earlier traffic opening.
WMA technologies are classified into three main categories based on their mechanism of action: organic additives, chemical additives, and foaming techniques. Each category has distinct performance characteristics, advantages, and limitations.
Organic WMA additives are typically waxes that reduce the viscosity of the asphalt binder at temperatures above their melting point. The most common organic additive is Sasobit®, a Fischer-Tropsch (FT) paraffin wax produced from coal gasification. The FT process converts synthesis gas (CO + H₂) into long-chain hydrocarbons in the presence of an iron or cobalt catalyst. Sasobit has a predominant hydrocarbon chain length of 40 to 115 carbon atoms — significantly longer than naturally occurring bituminous paraffin waxes (22 to 45 carbon atoms), which gives it a higher melting point (approximately 99°C / 210°F). Sasobit is completely soluble in asphalt binder at temperatures above 115°C (240°F) and is typically added at 1.0–4.0% by weight of binder, with 3.0% being the most common dosage.
Other notable organic additives include Asphaltan B® (Montan wax derived from lignite coal, used primarily in Germany at 2.0–4.0% by binder weight), Licomont BS® (a fatty acid amide from Clariant), and 3E LT / Ecoflex (proprietary wax technology from Colas, France).
The mechanism of action for organic wax additives has two temperature-dependent phases. Above the melting point (approximately 90–115°C depending on the specific wax), the wax dissolves in the binder and reduces its viscosity, enabling aggregate coating and compaction at lower temperatures. Below the melting point (at service temperatures), the wax crystallizes and forms a lattice structure within the binder, which increases the stiffness and deformation resistance of the pavement — providing improved rutting resistance compared to unmodified HMA. This dual behavior is a key advantage of organic wax additives. Organic additives typically achieve a temperature reduction of 20–30°C.
| Property | Sasobit (FT Wax) | Asphaltan B (Montan Wax) | Licomont BS (Fatty Acid Amide) |
|---|---|---|---|
| Base material | Fischer-Tropsch paraffin wax | Montan wax from lignite coal | Fatty acid amide |
| Chain length (C atoms) | 40–115 | 22–45+ | Not specified |
| Melting point | ~99°C (210°F) | ~99°C (210°F) | ~140°C |
| Typical dosage | 1.0–4.0% | 2.0–4.0% | 3.0% |
| Temperature reduction | 20–30°C (36–54°F) | 20–30°C | 20–30°C |
| Rutting resistance | Improved (crystallization) | Improved | Improved |
Chemical WMA additives do not reduce binder viscosity — instead, they work at the microscopic interface between aggregate particles and the asphalt binder. These additives are surfactants (surface-active agents) and emulsifiers that reduce the interfacial surface energy and internal friction between aggregate particles and the binder film. By reducing frictional forces at the aggregate-binder interface, chemical additives enable aggregate coating and mixture compaction at lower temperatures without changing the rheological properties of the binder itself.
The most widely used chemical additive in North America is Evotherm™, developed by MeadWestvaco (now part of Ingevity). Evotherm uses a chemical package delivered as an emulsion (dispersed asphalt technology) that provides aggregate coating, workability, adhesion, and improved compaction. The third generation Evotherm 3G (also branded as REVIX™) is water-free and relies on a reduction in internal friction between aggregate particles under high shear during mixing and high stress during compaction. Evotherm is dosed at 0.5–0.7% by weight of binder and can achieve temperature reductions of 20–40°C, with field tests demonstrating reductions of up to 55°C (100°F).
Rediset® (Akzo Nobel, now Nouryon) is a chemical additive that combines cationic surfactants with an organic additive component. It is dosed at 1.5–2.0% by weight of binder and achieves a temperature reduction of approximately 30°C. Rediset is used in the United States and Norway.
Other chemical WMA additives include Anova® (Cargill), a bio-based, non-hazardous, non-corrosive liquid derived from renewable resources. Anova is dosed at 0.2–0.7% by weight of binder and achieves temperature reductions of up to 44°C (80°F). According to Cargill’s technical documentation, Anova does not change the PG grade of the asphalt binder at recommended dosages and can be added at the terminal or injected in-line at the HMA plant.
Chemical additives offer several advantages: they do not alter binder rheology, they often improve adhesion and moisture resistance at the aggregate-binder interface, they are effective with a wide range of aggregate types, and they do not require significant plant modifications (they can be dosed directly into the binder line).
Foaming technologies reduce the effective viscosity of the asphalt binder by introducing small amounts of water into the hot binder, causing the water to vaporize into steam, which expands the binder volume and temporarily reduces its viscosity. The foaming effect is short-lived (typically lasting minutes), but sufficient for the mixing and compaction phases.
Foaming is achieved through two primary methods:
1. Direct Water Injection (Foaming Nozzles): This method injects a controlled amount of water directly into the hot binder via specially designed foaming nozzles. The water turns to steam upon contact with the hot binder (approximately 150–170°C), creating a large volume of foam that increases the binder’s effective volume by 10–20 times for a brief period. This technique requires plant modifications (foaming nozzle system, water metering, and control system) but does not require additives. Temperature reduction of 20–40°C is achievable. The WAM-Foam® process is a variant that uses a two-component binder system: a soft binder coats the aggregate first, followed by a hard foamed binder in a second mixing stage. This method was one of the earliest WMA technologies, developed in the late 1990s.
2. Water-Bearing Additives (Zeolites): This indirect foaming method uses hydrophilic minerals from the zeolite family (sodium aluminum silicate) that contain approximately 18–21% crystalline water by mass. When the zeolite is added to the mix at the same time as the binder, the water is released at temperatures above approximately 85–100°C (185–212°F), creating a controlled foaming effect. The foaming lasts for an extended period of 6–7 hours or until the mix temperature drops below 100°C.

Two commercial zeolite products are widely used:
A third indirect foaming method uses natural moisture from wet sand or RAP. In this sequential technique, coarse aggregate (approximately 80% of the mix) is dried and heated to 130–160°C, coated with binder, and then cold/wet fine aggregate or RAP is added. The moisture in the cold fraction contacts the hot binder and causes foaming, facilitating coating. This technique achieves a temperature reduction of approximately 20–40°C without any purchased additive.
Hybrid WMA technologies combine two or more approaches to achieve their effect. Examples include:
The temperature reduction achieved by WMA depends on the technology type, additive dosage, binder grade and source, aggregate type and moisture content, and plant configuration. The generally accepted temperature reduction ranges for each technology category are:
| WMA Technology | Typical Temperature Reduction | Typical Production Temperature Range |
|---|---|---|
| Organic (wax) additives | 20–30°C (36–54°F) | 120–150°C (248–302°F) |
| Chemical (surfactant) additives | 20–40°C (36–72°F) | 85–130°C (185–266°F) |
| Foaming – water injection | 20–40°C (36–72°F) | 110–140°C (230–284°F) |
| Foaming – zeolites | 28–39°C (50–70°F) | 110–140°C (230–284°F) |
| Emulsion-based (Evotherm) | Up to 55°C (100°F) | 85–115°C (185–239°F) |
| Bio-based (Anova) | Up to 44°C (80°F) | 85–130°C (185–266°F) |
The temperature reduction is typically expressed relative to the equivalent HMA production temperature for the same mix design. It is important to note that achieving the full temperature reduction potential requires optimization of additive dosage, mixing time, and plant settings for each specific combination of materials.
The use of WMA additives has implications for asphalt binder grade selection that must be carefully considered during mix design. Three factors interact:
1. Reduced Binder Aging: The lower production and storage temperatures of WMA result in less oxidative aging of the binder during manufacturing compared to HMA. This means the binder in the final WMA pavement will be softer than an equivalent HMA binder. While this softer binder can improve thermal cracking resistance and fatigue resistance, it may also reduce rutting resistance if not accounted for. This is generally considered a net benefit because it extends pavement fatigue life and reduces low-temperature cracking.
2. Organic Wax Crystallization at Service Temperatures: For organic (wax) additives, the wax crystallizes in the binder at temperatures below its melting point (approximately 90–100°C / 194–212°F). This crystallization creates a lattice structure that stiffens the binder at typical pavement service temperatures (up to 60–70°C / 140–158°F). The stiffening effect increases rutting resistance, but may also increase low-temperature stiffness and potentially reduce thermal cracking resistance. For this reason, when using organic wax additives, some agencies recommend binder grade bumping — selecting a binder that is one grade lower (softer) in the high-temperature grade to compensate for the wax stiffening effect. For example, an HMA that would use PG 70-22 might use PG 64-28 in a wax-based WMA. However, AASHTO M 320 and Superpave specifications can accommodate this through binder testing with the additive.
3. Chemical and Foaming Additives: Chemical additives (surfactants, emulsifiers) and foaming technologies (zeolites, water injection) generally do not change the binder’s performance grade at recommended dosages. Detailed rheological testing, including Dynamic Shear Rheometer (DSR) and Bending Beam Rheometer (BBR) testing of binder with and without the additive, is recommended to verify the PG grade. For zeolites (e.g., Advera), the manufacturer explicitly states that the material does not affect PG grade because it is an inorganic material that remains in the mix as fine mineral filler after water release.
Moisture sensitivity (also called moisture susceptibility or stripping) refers to the loss of adhesion between the asphalt binder and aggregate due to the presence of water. For WMA, early concerns focused on the possibility that lower production temperatures could lead to:
However, extensive research and field experience have demonstrated that properly designed WMA can meet or exceed HMA moisture resistance, provided that appropriate measures are taken. These measures include:
Proper quality control testing during WMA production, including TSR testing on plant-produced mixtures, ensures that moisture susceptibility requirements are met.
Achieving target in-place density (typically 92–97% of maximum theoretical density, corresponding to 3–8% air voids depending on the application) is essential for asphalt pavement performance. Low density leads to high air voids, which allow water and air ingress, leading to moisture damage, oxidation, raveling, cracking, and premature failure.
WMA offers several compaction-related advantages over HMA:
The compaction procedure for WMA is similar to HMA, with adjustments to the temperature window based on the specific additive and mixture. Quality control during WMA compaction typically includes:
WMA is fully compatible with and complementary to the use of Reclaimed Asphalt Pavement (RAP) . The synergy between WMA and RAP content is well-documented and provides several benefits:
| Parameter | HMA without RAP | HMA with RAP | WMA with RAP |
|---|---|---|---|
| Production temperature | 150–190°C | 150–190°C | 100–150°C |
| Typical RAP content | 0% | 15–30% | 20–50%+ |
| Virgin binder requirement | 100% | 70–85% | 50–80% |
| Fuel energy consumption | Baseline | ~Baseline | 5–12% reduction |
| CO₂ emissions | Baseline | 10–20% reduction | 20–40% reduction |
| Virgin aggregate required | 100% | 70–85% | 50–80% |
Long-term field performance data for WMA pavements has been accumulating since the early 2000s, with many sections now exceeding 15–20 years of service. The key findings from long-term performance studies include:
Rutting Performance: WMA pavements generally exhibit equivalent or better rutting resistance compared to HMA controls. WMA with organic wax additives (Sasobit, Asphaltan B) benefits from the wax crystallization stiffening effect, which increases resistance to permanent deformation at service temperatures. Chemical additive and foaming WMA pavements have shown comparable rutting to HMA when the same binder grade is used.
Cracking Performance: WMA pavements often show improved cracking resistance compared to HMA, particularly for thermal cracking and fatigue cracking. This improvement is attributed to the reduced binder aging during production — the binder in WMA is less oxidized and therefore more flexible at low temperatures. However, cracking performance can be climate-dependent. Research from the Long-Term Pavement Performance (LTPP) Specific Pavement Studies 10 (SPS-10) program indicates that cracking distress is more of a concern in wet climatic zones for WMA, while rutting is more significant in dry climates. The SPS-10 study analyzed field performance of WMA overlays across multiple US states.
Moisture Damage: Early WMA field trials occasionally reported moisture damage in sections where anti-strip additives were not used or where compaction was inadequate. However, the majority of properly designed WMA pavements (with anti-strip treatment and adequate compaction) have demonstrated satisfactory long-term moisture resistance equivalent to HMA.
Aging and Stiffness: Field cores extracted from WMA pavements after extended service show lower stiffness and better ductility than adjacent HMA sections. This confirms that the reduced binder aging during production translates into longer pavement life, particularly in terms of fatigue and thermal cracking.
Overall Performance Rating: The consensus from multiple long-term studies (including Louisiana DOTD, NCAT Test Track, LTPP SPS-10, and European field trials) is that WMA pavements perform equivalently to HMA pavements when designed, produced, and compacted according to specifications tailored to the specific WMA technology and materials.
The use of WMA on airport pavements is governed by the FAA Advisory Circular 150/5370-10 (Standards for Specifying Construction of Airports), specifically Item P-401 (Asphalt Mix Pavements). The FAA has evaluated WMA for airfield applications and has determined that WMA is a viable alternative to HMA for use on heavily trafficked airfield pavements, subject to meeting all standard P-401 requirements.
The Unified Facilities Guide Specification (UFGS) 32 12 15 has been updated to accommodate WMA technologies. Key requirements for WMA use under FAA P-401 include:
The FAA has conducted specific research on WMA for airfield pavements through the Airport Technology Research & Development Branch, including studies at the National Airport Pavement Test Facility (NAPTF) and the William J. Hughes Technical Center. These studies have demonstrated that WMA can achieve equivalent structural performance to HMA under aircraft loading. The study “Warm-Mix Asphalt for Airfield Pavements” (Mejias-Santiago, FAA) concluded that WMA is recommended as a viable alternative to HMA for use on heavily trafficked airfield pavements.
For airport pavement engineers and inspectors, the key considerations for WMA acceptance include verifying that:
WMA is a cornerstone technology for sustainable pavement construction. Its sustainability benefits span environmental, economic, and social dimensions:
The Life Cycle Assessment (LCA) of WMA consistently demonstrates environmental benefits compared to HMA across multiple impact categories:
The European Asphalt Pavement Association (EAPA) and National Asphalt Pavement Association (NAPA) both have position papers supporting WMA as a key sustainability strategy. The EAPA Position Paper “The Use of Warm Mix Asphalt” and NAPA’s “How Warm-Mix Asphalt Supports DOT Goals for Sustainability and Resilience” (June 2024) provide comprehensive guidance for agencies considering WMA adoption.
WMA is accommodated within existing asphalt specifications through:

| Technology | Mechanism | Temperature Reduction | Effect on Binder | Effect on Performance |
|---|---|---|---|---|
| Organic wax (Sasobit, Asphaltan B) | Viscosity reduction above melting point; crystallization below | 20–30°C (36–54°F) | Stiffens at service temperatures | Improved rutting resistance; may require binder grade adjustment |
| Chemical surfactant (Evotherm, Rediset, Anova) | Interfacial friction reduction; improved coating | 20–40°C (36–72°F) | No significant change | Improved adhesion and moisture resistance; improved compaction |
| Direct water injection (Foaming nozzles, WAM-Foam) | Temporary viscosity reduction through binder expansion | 20–40°C (36–72°F) | No change after foaming subsides | Equivalent to HMA; requires moisture monitoring |
| Water-bearing zeolites (Aspha-Min, Advera) | Controlled foaming through crystalline water release | 28–39°C (50–70°F) | No change; zeolite remains as mineral filler | Equivalent to HMA; extended workability (6–7 hours) |
| Bio-based (Anova) | Chemical surface activity | Up to 44°C (80°F) | No change (at recommended dosage) | Improved compaction; no PG grade change |
| Hybrid (Combined technologies) | Multiple mechanisms | 20–40°C (36–72°F) | Technology-dependent | Technology-dependent |
The selection of the appropriate WMA technology depends on project-specific factors including: local availability of additives and equipment, aggregate type and mineralogy, binder grade and source, RAP content, climate conditions (ambient temperature and humidity), plant configuration (batch vs. drum, ability to add foaming nozzles or injection systems), and specification requirements of the governing agency.
For airport pavements subject to FAA P-401 or equivalent specifications, the additional requirement for performance testing (Hamburg wheel-track, SCB, DCT) and quality control verification (TSR, density, air voids) should guide technology selection toward those with established field performance data on airfield pavements.
TarmacView provides AI-powered pavement surface analysis to help you assess WMA and HMA pavement condition, detect early distress, and manage your asphalt assets — from airport runways to highway networks.
Warm Mix Asphalt (WMA) technologies reduce HMA production and placement temperatures by 20-40°C through additives or processes: organic waxes (Sasobit), chemica...
Hot Mix Asphalt (HMA) is the standard flexible pavement material produced by heating and mixing aggregate and asphalt binder at 150–180°C, then placing and comp...
Foamed asphalt is produced by injecting a small amount of cold water into hot asphalt binder, causing it to expand dramatically into a foam that temporarily inc...