Preparation and Rheological Properties of Waterborne Epoxy Resin Emulsified Asphalt
Abstract
1. Introduction
2. Preparation of Waterborne Epoxy Resin Emulsified Asphalt
2.1. Experimental Materials and Instruments
2.1.1. Preparation of Experimental Materials
- (1)
- Base asphalt: 90# road petroleum asphalt is selected. The manufacturer is Shandong Jingbo Petrochemical Co., Ltd. (Binzhou, China). This asphalt has good ductility and adhesion and is suitable for the preparation of emulsified asphalt in road engineering. Its specific performance parameters are shown in Table 1.
- (2)
- Emulsifier: The JY-R2 type cationic emulsifier produced by Jiangsu Jinyang New Material Technology Co., Ltd. is used. (Yixing, China). The emulsifier is a light yellow transparent liquid, which is easily soluble in water at room temperature. The active ingredient content is (55 ± 2)%, which has the characteristics of high emulsification efficiency and good emulsion stability. It can form a strong adsorption film on the surface of asphalt particles and effectively reduce the interfacial tension between oil and water.
- (3)
- Waterborne epoxy resin: Grafted modified E-44 produced by Guangzhou Epoxy New Material Co., Ltd. (Guangzhou, China) is selected. This resin is prepared by grafting hydrophilic groups onto the E-44 epoxy resin molecular chain. It has the high strength and high corrosion resistance of epoxy resin and the environmental protection of waterborne materials. Its performance indicators are shown in Table 2.
- (4)
- Curing agent: The XK-801 type amine waterborne curing agent produced by Shanghai Sika Chemical Co., Ltd. (Shanghai, China) was selected. It is a light yellow viscous liquid. It has excellent compatibility with the grafted modified E-44 waterborne epoxy resin used in this experiment. The curing speed is moderate. The cured product has good hardness and toughness. The curing time (25 °C) is 4 h. The solid content is ≥50%. The pH value is 7~9.
- (5)
- Distilled water: The distilled water used in the experiment was prepared in the laboratory, with a conductivity ≤ 10 μS/cm, and was used to prepare emulsifier aqueous solution and adjust the viscosity of the system.
2.1.2. Preparation of Experimental Instruments and Equipment
2.2. Preparation Process of Waterborne Epoxy Resin Emulsified Asphalt
2.2.1. Mix Proportion Design
2.2.2. Preparation Process
- (1)
- Raw material pretreatment: The matrix asphalt was heated at 135 °C for 30 min to melt and dehydrate. This temperature was selected based on the asphalt’s Penetration Index (PI = −0.82) and the manufacturer’s recommended construction temperature range for 90# road petroleum asphalt, which is typically 130–140 °C. A temperature of 135 °C ensures complete fluidity without causing significant thermal aging (as verified by preliminary thermogravimetric analysis showing negligible mass loss below 150 °C). The emulsifier was added to distilled water and stirred at 60 °C and 500 r/min for 15 min to prepare an emulsifier aqueous solution; the waterborne epoxy resin and curing agent were preheated at 60 °C for 10 min to facilitate uniform mixing later.
- (2)
- Preparation of emulsified asphalt: The pretreated matrix asphalt was slowly added to the preheated emulsifier aqueous solution, and the high-speed shear emulsifier was started at the same time. The shear temperature was controlled at 65 °C, the shear speed was 10,000 r/min, and the shear time was 20 min. This speed was determined through preliminary optimization tests (range: 5000–12,000 r/min), where 10,000 r/min produced the smallest emulsion droplet size (D50 ≈ 3.2 μm) and the most uniform dispersion, as observed by optical microscopy. Higher speeds led to air entrapment, while lower speeds resulted in incomplete emulsification. This value is also consistent with the typical shear rate used for preparing cationic emulsified asphalt in previous studies.
- (3)
- Preparation of waterborne epoxy resin emulsion: The preheated waterborne epoxy resin was added to an appropriate amount of distilled water, and the high-speed shear emulsifier was started. At 60 °C, the emulsifier was sheared at 8,000 r/min for 10 min to prepare a uniform waterborne epoxy resin emulsion. This rotational speed was chosen based on the viscosity (350 mPa·s at 25 °C) and solid content (50%) of the waterborne epoxy resin. Lower speeds (e.g., 5000 r/min) failed to fully break the resin agglomerates, whereas higher speeds (e.g., 10,000 r/min) induced excessive foaming and slight thermal heating [16]. The value of 8,000 r/min was identified as optimal from pre-experiments evaluating emulsion stability after 24 h (no visible stratification).
- (4)
- Preparation of composite system: The prepared waterborne epoxy resin-curing agent mixed emulsion was slowly added to the heat-insulating emulsified asphalt, while stirring continuously at a speed of 500 r/min. The stirring temperature was controlled at 60 °C, and the stirring time was 25 min. During the stirring process, the remaining distilled water was added dropwise at a rate of 5–10 mL/min to adjust the viscosity of the emulsion to a target range of 500–800 mPa·s. The viscosity was monitored in real time using a rotational viscometer (Brookfield DV-II + Pro, spindle No. 21) at 60 °C and a shear rate of 50 s−1. The water addition was stopped once the viscosity stabilized within this range, which typically required 80–120 mL of water depending on the initial solid content of each formulation. This viscosity range was selected based on preliminary experiments to ensure sufficient workability for subsequent specimen preparation (e.g., uniform coating on aggregate surfaces) while avoiding excessive dilution that could compromise mechanical properties. The uniformity was preliminarily assessed by visual observation (no visible phase separation or flocculation within 30 min after stirring).
- (5)
- Curing and storage: The prepared waterborne epoxy resin emulsified asphalt emulsion was placed in a 60 °C constant temperature water bath for curing for 30 min, and then naturally cooled to room temperature. This curing protocol was designed to achieve initial gelation and handling strength rather than complete curing. According to the technical datasheet of the XK-801 amine curing agent, the full curing time at 60 °C is approximately 4 h. The 30 min treatment at 60 °C was selected to (i) accelerate the initial crosslinking reaction without causing water evaporation or emulsion destabilization, (ii) ensure that the specimens could be demolded without deformation, and (iii) maintain a consistent thermal history across all samples before subsequent storage. Complete curing was reached during the subsequent 24 h storage at 25 °C, as verified by preliminary experiments showing no further increase in Marshall stability or epoxy conversion (measured by FTIR) after 24 h. After sealing, it was stored in a cool and dry place with the storage temperature controlled at about 25 °C. It can be used for subsequent performance testing after 24 h.
2.2.3. Stability Evaluation Method
- (1)
- Storage stability test: Immediately after preparation, each emulsion sample (approximately 200 mL) was poured into a graduated glass cylinder and stored at 25 ± 1 °C for 7 days without disturbance. The storage stability (SS) was calculated as the percentage of sediment volume at the bottom of the cylinder relative to the total volume after 7 days, following Equation (1):
- (2)
- Particle size distribution analysis: A laser particle size analyzer (Mastersizer 3000, Malvern Panalytical, Westborough, MA, USA) was used to measure the droplet size distribution of the emulsion at 0 h and 24 h after preparation. The uniformity of the system was evaluated by the change in D [4,3] (volume-weighted mean diameter). An increase in D [4,3] of less than 10% over 24 h was taken as evidence of good colloidal stability, indicating no significant coalescence or flocculation.
- (3)
- Zeta potential measurement: The zeta potential of the fresh emulsions was measured using a ZetaPlus zeta potential analyzer (Brookhaven Instruments, Nashua, NH, USA) at 25 °C. Each emulsion sample was diluted with distilled water at a volume ratio of 1:100 to avoid multiple scattering effects. Three replicate measurements were performed for each specimen, and the average zeta potential value was reported. A zeta potential with an absolute value greater than 30 mV is generally considered indicative of sufficient electrostatic repulsion for good colloidal stability.
- (4)
- Demulsification behavior test: The demulsification time of each emulsion was evaluated using the calcium chloride (CaCl2) demulsification test according to the Chinese standard JTG E20-2011 (T 0653) [17]. Specifically, 10 mL of the emulsion was mixed with 10 mL of 0.5% CaCl2 solution at 25 °C, and the time required for complete phase separation (i.e., the appearance of a clear water layer and coagulated asphalt) was recorded as the demulsification time. A shorter demulsification time indicates faster breakage, which is desirable for rapid strength gain in pavement construction. The test was repeated three times for each specimen, and the average values are reported.
2.2.4. Curing Degree Verification
- (1)
- Epoxy conversion measurement: Fourier-transform infrared spectroscopy (FTIR, Nicolet iS50, Thermo Fisher, Waltham, MA, USA) was used to monitor the disappearance of the epoxy peak at 915 cm−1 (oxirane ring) over time. For the WER-EA-20 specimen, the conversion reached 92.5% after 24 h at 25 °C and 96.8% after 72 h, indicating that near-complete curing (>90%) is achieved within 24 h. No significant change (>2%) was observed between 24 h and 72 h, confirming that the 24 h storage is sufficient for practical full curing.
- (2)
- Mechanical property saturation: Marshall stability of WER-EA-20 specimens cured for 12 h, 24 h, 48 h, and 72 h at 25 °C (after the initial 30 min at 60 °C) was tested. The stability increased from 18.3 kN (12 h) to 22.1 kN (24 h), with further increases of less than 2% at 48 h (22.4 kN) and 72 h (22.5 kN). This plateau confirms that the curing reaction is substantially complete after 24 h.
2.3. Testing and Characterization Methods
2.3.1. Rheological Properties Test
- (1)
- High-temperature rheological performance test: The test was conducted using a dynamic shear rheometer (DSR). The test temperatures were selected as 45 °C, 50 °C, 55 °C, 60 °C, 65 °C, 70 °C, and 75 °C. The test frequency was 10 rad/s (simulating traffic loading frequency). A 25 mm parallel plate geometry with a 1 mm gap was used. The specimen was heated to the test temperature and held for 10 min to achieve thermal equilibrium. A sinusoidal oscillatory shear load was then applied, and the phase angle δ and complex shear modulus G* at each temperature were recorded.
- (2)
- Intermediate-temperature rheological performance test: The test was conducted using a dynamic shear rheometer (DSR). The test temperatures were selected as 15 °C, 20 °C, 25 °C, 30 °C, 35 °C, 40 °C, and 45 °C. The test frequency was 10 rad/s. A 25 mm parallel plate geometry with a 1 mm gap was used. The specimen was held at a constant temperature for 10 min before testing. A sinusoidal oscillatory shear load was applied, and the phase angle δ and complex shear modulus G* at each temperature were recorded.
- (3)
- Low-temperature rheological performance test: The test was conducted using a dynamic shear rheometer (DSR) equipped with 4 mm parallel plates and a 1 mm gap. The test temperatures were selected as −30 °C, −25 °C, −20 °C, −15 °C, −10 °C, −5 °C, and 0 °C. A frequency sweep mode was applied over a range of 0.628 to 62.8 rad/s (equivalent to 0.1 to 10 Hz). The specimen was cooled to the target temperature and held for 10 min to achieve thermal equilibrium. A sinusoidal oscillatory shear load was then applied, and the phase angle δ and complex shear modulus G* at each temperature were recorded.
2.3.2. Resistance to Permanent Deformation Test
2.3.3. Fatigue Characteristics Test
2.3.4. Crack Resistance Test
2.3.5. Bonding Performance Test
2.3.6. Strength Development Test
2.3.7. Water Resistance Test
2.3.8. Performance Comparison Test
- (1)
- Softening point: The ring and ball method was used to test and record the temperature at which the specimen softened.
- (2)
- Penetration: Tested at 25 °C, 100 g, and 5 s to reflect the material hardness.
- (3)
- Ductility: Tested at 15 °C and 5 cm/min to evaluate low-temperature ductility.
- (4)
- Storage stability: Stored at 50 °C for 7 days, the mass change rate before and after storage was tested to evaluate the emulsion stability.
- (5)
- Mixing temperature: The viscosity at different temperatures was tested using a rotational viscometer to determine the appropriate mixing temperature.
- (6)
- Aging performance: The mass change rate and penetration ratio after heating were tested using a thin film oven heating test.
3. Study of the Rheological Properties of Waterborne Epoxy Resin Emulsified Asphalt
3.1. Analysis of Rheological Properties
3.2. Analysis of Resistance to Permanent Deformation
3.3. Fatigue Characteristics
3.4. Crack Resistance
3.5. Low-Temperature Creep Stiffness and m-Value
3.6. Effect of Waterborne Epoxy Resin on Emulsion Stability and Demulsification Behavior
4. Comparative Analysis of Results
4.1. Basic Road Performance Test
4.1.1. Bonding Performance
4.1.2. Strength Development
4.1.3. Water Resistance
4.2. Performance Comparison and Advantage Analysis
4.3. Comparative Assessment: Cost, Carbon Footprint, and Performance
5. Conclusions
- (1)
- A stable waterborne epoxy resin emulsified asphalt can be successfully prepared by a two-step process of “preparing emulsified asphalt first and then composite waterborne epoxy resin emulsion”.
- (2)
- The optimal process parameters are: base asphalt heating temperature of 135 °C, emulsifier aqueous solution temperature of 60 °C, epoxy resin emulsion shear speed of 8000 r/min, composite system stirring temperature of 60 °C, and stirring time of 25 min. This process can ensure that the components are fully mixed and avoid emulsion stratification and demulsification.
- (3)
- The incorporation of waterborne epoxy resin can significantly optimize the viscoelastic properties of emulsified asphalt and improve its resistance to deformation. The higher the dosage, the more significant the optimization effect. The WER-EA-20 specimen with 20% dosage showed the best rheological properties in the entire temperature range of high temperature, medium temperature and low temperature, with the smallest phase angle δ and the highest proportion of elastic components, which provides a guarantee for the service stability of the pavement under different climatic conditions.
- (4)
- Waterborne epoxy resin modification can simultaneously improve the resistance to permanent deformation, fatigue characteristics and crack resistance of emulsified asphalt. After seven creep–recovery cycles at 60 °C and 3.2 kPa stress, the creep–recovery rate of WER-EA-20 still reached 33%, the fatigue life under 2.1 MPa shear stress reached 15,000 cycles, and the fracture strength at −10 °C was 0.92 MPa and the fracture energy was 21.4 J, which is significantly improved compared with the unmodified specimen. It can effectively solve the problems of high-temperature rutting, low-temperature cracking and fatigue damage of road surface. In addition, BBR results indicated that WER-EA-20 exhibited the lowest creep stiffness and highest m-value among all specimens at low temperatures, fully satisfying the Superpave low-temperature cracking criteria.
- (5)
- Waterborne epoxy resin emulsified asphalt has excellent road performance. The pull-out strength of WER-EA-20 reaches 0.86 MPa. After 37 days of curing, the Marshall stability is 22.5 kN and the splitting strength is 1.36 MPa. After 40 freeze–thaw cycles, the freeze–thaw splitting strength ratio exceeds 75%. The thin-film oven test shows that WER-EA-20 achieves a penetration ratio of 90.5% and a mass loss of only 0.22% after aging, demonstrating superior aging resistance compared to UEA-0 (62.5%, −0.82%) and SBR-EA (73.8%, −0.56%). Compared with SBR-modified emulsified asphalt, it has a higher softening point, lower mixing temperature, and better anti-aging performance.
- (6)
- The addition of waterborne epoxy resin slightly reduces the zeta potential (from +38.5 mV to +29.6 mV) and increases the mean droplet size (from 3.8 μm to 5.3 μm), but significantly improves the 7-day storage stability (SS decreasing from 1.85% to 0.23%) due to enhanced steric stabilization. The demulsification time prolongs from 45 s to 78 s with 20% WER, which still allows for adequate workability while maintaining satisfactory early strength development.
6. Industry Implications
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Conflicts of Interest
References
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| Technical Index | Unit | Test Result |
|---|---|---|
| Density (25 °C) | g/cm3 | 1.013 |
| Penetration (25 °C, 100 g, 5 s) | 0.1 mm | 88 |
| Softening Point (Ring and Ball Method) | °C | 46.5 |
| Ductility (15 °C, 5 cm/min) | cm | >100 |
| Ductility (10 °C, 5 cm/min) | cm | 38.6 |
| Penetration Index (PI) | - | −0.82 |
| Mass Change Rate After Thin Film Oven Test | % | 0.32 |
| Penetration Ratio After Thin Film Oven Test (25 °C) | % | 68.5 |
| Technical Index | Unit | Test Result |
|---|---|---|
| Density (25 °C) | g/cm3 | 1.07 |
| Solid Content | % | 50 |
| Epoxy Value | eq/100 g | 0.16 |
| Epoxy Equivalent Weight | g/eq | 625 |
| Viscosity (25 °C, Rotational Viscometer) | mPa·s | 350 |
| pH Value | - | 7.2 |
| Appearance | - | Milky white uniform emulsion |
| Storage Stability (50 °C, 7 d) | % | 0.8 |
| Equipment Name (Model) | Core Parameters | Manufacturer |
|---|---|---|
| High-Speed Shear Emulsifier (FA25) | Rotational speed: 0~12,000 r/min; shear head diameter: 50 mm; power: 1.5 kW; heating: water bath, room temperature ~100 °C | Shanghai Fluko Fluid Machinery Manufacturing Co., Ltd. (Shanghai, China) |
| Colloid Mill (JM-L80) | Rotational speed: 3000 r/min; grinding gap: 0~50 μm; power: 2.2 kW; feed particle size: ≤2 mm | Zibo Longda Machinery Manufacturing Co., Ltd. (Zibo, China) |
| Electronic Balance (PL6001-L) | Measuring range: 0~5000 g; accuracy: 0.1 g; repeatability error: ±0.1 g | Mettler Toledo Instruments (Shanghai) Co., Ltd. (Shanghai, China) |
| Constant Temperature Water Bath (HH-S4) | Temperature: room temperature ~100 °C; temperature control accuracy: ±0.5 °C; capacity: 5 L; power: 1.5 kW | Shanghai Precision Instruments & Meters Co., Ltd. (Shanghai, China) |
| Oven (DHG-9070A) | Temperature: room temperature ~300 °C; temperature control accuracy: ±1 °C; power: 2.0 kW | Shanghai Yiheng Scientific Instruments Co., Ltd. (Shanghai, China) |
| Dynamic Shear Rheometer (DSR, MCR 302) | Temperature: −40~100 °C; frequency: 0.01~100 Hz; stress: 0.1~1000 Pa; test modes: oscillatory shear, creep–recovery | Anton Paar (China) Co., Ltd. (Shanghai, China) |
| Bending Beam Rheometer (BBR, AR 2000ex) | Temperature: −40~25 °C; loading: constant load; test time: 0~3600 s; displacement accuracy: 0.01 mm | TA Instruments (New Castle, DE, USA) |
| Tensile Tester (WDW-50) | Maximum load: 50 kN; loading speed: 0.1~50 mm/min; accuracy: class 0.5; displacement range: 0~50 mm | Jinan Shijin Group Co., Ltd. (Jinan, China) |
| Marshall Stability Tester (LM-2) | Maximum load: 50 kN; loading speed: 50 mm/min; stability accuracy: ± 0.1 kN | Beijing Aerospace Keyu Testing Instruments Co., Ltd. (Beijing, China) |
| Splitting Tester (SYD-0716) | Maximum load: 100 kN; loading speed: 1 mm/min; accuracy: class 0.5; equipped with low-temperature environmental chamber: −30 °C~room temperature | Shanghai Highway Engineering Testing Instruments Co., Ltd. (Shanghai, China) |
| Freeze–Thaw Test Chamber (DW-40) | Temperature: −40~60 °C; temperature control accuracy: ±1 °C; freeze–thaw cycles: programmable; working chamber volume: 100 L | Zhongke Aobo (Beijing) Technology Co., Ltd. (Beijing, China) |
| Rotational Viscometer (DV-II + Pro) | Rotational speed: 0.3~100 r/min; measuring range: 1~1 × 106 mPa·s; temperature: room temperature ~150 °C; temperature control accuracy: ±0.1 °C | Brookfield (New York, NY, USA) Co., Ltd. |
| Ring and Ball Softening Point Tester (SYD-2806E) | Temperature: room temperature ~150 °C; temperature control accuracy: ±0.5 °C; heating rate: 5 °C/min; steel ball mass: 3.5 g | Shanghai Changji Geological Instruments Co., Ltd. (Shanghai, China) |
| Penetrometer (SYD-2801E) | Measuring range: 0~500 × 0.1 mm; accuracy: ±1 × 0.1 mm; loading mass: 100 g; loading time: 5 s | Tianjin Huayin Test Instruments Co., Ltd. (Tianjin, China) |
| Ductility Tester (SYD-4508) | Tensile speed: 5 cm/min; measuring range: 0~150 cm; temperature control accuracy: ±0.5 °C; water tank volume: 50 L | Shanghai Suying Test Instruments Co., Ltd. (Shanghai, China) |
| Thin Film Oven (SYD-0609) | Temperature: room temperature ~200 °C; temperature control accuracy: ±1 °C; working chamber size: 300 × 300 × 200 mm; wind speed: 2.5 m/s | Beijing Zhongke Luda Test Instruments Co., Ltd. (Beijing, China) |
| Specimen No. | UEA-0 | WER-EA-5 | WER-EA-10 | WER-EA-20 | |
|---|---|---|---|---|---|
| Dosage | |||||
| Waterborne Epoxy Resin/g | 0 | 50 | 100 | 200 | |
| Emulsified Asphalt/g | 1000 | 1000 | 1000 | 1000 | |
| Curing Agent/g | 0 | 42.5 | 85 | 170 | |
| Emulsifier/g | 20 | 20 | 20 | 20 | |
| Distilled Water/g | 650 | 627.5 | 605 | 560 | |
| Total Mass/g | 1670 | 1740 | 1810 | 1950 | |
| Solid Content/% | 60 | 60.1 | 60.2 | 60.3 | |
| Temperature/°C | Performance Indicators | UEA-0 | WER-EA-5 | WER-EA-10 | WER-EA-20 |
|---|---|---|---|---|---|
| −10 | Fracture Strength/MPa | 0.42 | 0.58 | 0.75 | 0.92 |
| Fracture Elongation/cm | 6.8 | 8.5 | 10.3 | 12.6 | |
| Fracture Energy/J | 7.2 | 10.8 | 15.6 | 21.4 | |
| −15 | Fracture Strength/MPa | 0.56 | 0.73 | 0.91 | 1.12 |
| Fracture Elongation/cm | 4.3 | 5.7 | 7.2 | 9.5 | |
| Fracture Energy/J | 5.1 | 7.9 | 11.8 | 16.5 |
| Specimen | Temp.(°C) | Creep Stiffness S(t) (MPa) | m-Value |
|---|---|---|---|
| UEA-0 | −12 | 285 | 0.31 |
| −18 | 412 | 0.24 | |
| −24 | 598 | 0.19 | |
| WER-EA-5 | −12 | 258 | 0.34 |
| −18 | 376 | 0.27 | |
| −24 | 545 | 0.22 | |
| WER-EA-10 | −12 | 224 | 0.38 |
| −18 | 331 | 0.31 | |
| −24 | 478 | 0.26 | |
| WER-EA-20 | −12 | 196 | 0.42 |
| −18 | 289 | 0.36 | |
| −24 | 421 | 0.31 |
| Specimen | Zeta Potential (mV) | SS After 7 Days (%) | D [4,3] (μm) | Demulsification Time (s) |
|---|---|---|---|---|
| UEA-0 | +38.5 ± 2.1 | 1.85 | 3.8 | 45 ± 3 |
| WER-EA-5 | +36.2 ± 1.8 | 0.68 | 4.2 | 52 ± 4 |
| WER-EA-10 | +33.4 ± 1.5 | 0.45 | 4.7 | 62 ± 5 |
| WER-EA-20 | +29.6 ± 1.2 | 0.23 | 5.3 | 78 ± 6 |
| Strength Ratio Type | Pull-Out Strength/MPa | Peak Displacement/mm | Tensile Failure Mode |
|---|---|---|---|
| UEA-0 | 0.32 | 0.85 | Interface Failure (complete separation between aggregate and asphalt) |
| WER-EA-5 | 0.48 | 1.02 | Partial Interface Failure (a small amount of asphalt remains on the aggregate surface) |
| WER-EA-10 | 0.65 | 1.23 | Mixed Failure (coexistence of interface failure and asphalt cohesive failure) |
| WER-EA-20 | 0.86 | 1.45 | Asphalt Cohesive Failure (asphalt fractures itself and completely remains on the aggregate surface) |
| Specimen Type | UEA-0 | SBR-EA (4% SBR) | WER-EA-5 (5%WER) | WER-EA-10 (10%WER) | WER-EA-20 (20%WER) |
|---|---|---|---|---|---|
| Softening Point/°C | 46.2 | 52.5 | 55.8 | 61.3 | 68.7 |
| Penetration/(0.1 mm) | 85.3 | 68.7 | 62.4 | 53.2 | 41.6 |
| Ductility/cm | 28.6 | 42.3 | 36.8 | 39.5 | 45.2 |
| Storage Stability/% | 1.85 | 0.92 | 0.68 | 0.45 | 0.23 |
| Optimum Mixing Temperature/°C | 65 | 60 | 58 | 55 | 52 |
| Mass Change Rate After Aging/% | −0.82 | −0.56 | −0.43 | −0.31 | −0.22 |
| Penetration Ratio After Aging/% | 62.5 | 73.8 | 78.6 | 84.2 | 90.5 |
| Modifier Type | Cost (Relative) | Carbon Footprint | Recyclability | High-Temp Performance | Low-Temp Flexibility |
|---|---|---|---|---|---|
| Crumb Rubber | Low | Low (waste reuse) | Good | Moderate | Excellent |
| SBR Polymer | Medium | Medium | Good | Moderate | Good |
| Slag | Low | Low (industrial byproduct) | Excellent | Low | Poor |
| WER-EA-20 | Medium–High | High (epoxy production) | Poor | Excellent | Moderate |
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Wu, S.; Chen, H.; Zheng, S.; Dong, Y.; Zhang, W. Preparation and Rheological Properties of Waterborne Epoxy Resin Emulsified Asphalt. Materials 2026, 19, 2493. https://doi.org/10.3390/ma19122493
Wu S, Chen H, Zheng S, Dong Y, Zhang W. Preparation and Rheological Properties of Waterborne Epoxy Resin Emulsified Asphalt. Materials. 2026; 19(12):2493. https://doi.org/10.3390/ma19122493
Chicago/Turabian StyleWu, Siyu, Huaxin Chen, Suining Zheng, Yonglu Dong, and Wenlan Zhang. 2026. "Preparation and Rheological Properties of Waterborne Epoxy Resin Emulsified Asphalt" Materials 19, no. 12: 2493. https://doi.org/10.3390/ma19122493
APA StyleWu, S., Chen, H., Zheng, S., Dong, Y., & Zhang, W. (2026). Preparation and Rheological Properties of Waterborne Epoxy Resin Emulsified Asphalt. Materials, 19(12), 2493. https://doi.org/10.3390/ma19122493

