Open Access Article
Huifen Wang
*ab,
Xiongjun Liua,
Xiao Hana and
Lijuan Yuana
aAcademy of Science and Technology, Jiangsu Shangshang Cable Group Co., Ltd., Liyang 213300, China. E-mail: wanghuifen0860@163.com
bSchool of Chemical Engineering and Technology, China University of Mining and Technology, Xuzhou 221000, China
First published on 3rd February 2026
This study systematically investigates the influence of ATH particle size characteristics (D50 and SPAN) on the flame-retardant performance of ATH/polyolefin composites, and focuses on discussing the potential roles of interface properties and thermal decomposition behavior. Comprehensive analysis reveals that an ATH median particle size (D50) of 2.28 µm, coupled with a SPAN value of 2.19, achieves an optimal balance, facilitating uniform dispersion and strong interfacial adhesion within the polyolefin matrix. This optimal interface not only promotes the formation of a protective char barrier during combustion, as evidenced by a distinct bimodal HRR profile and significantly reduced peak HRR and total heat release values of 129.86 kW m−2 and 56.57 MJ m−2, respectively, but also enables the composite material to have the highest tensile strength and elongation at break, demonstrating the synergistic enhancement of flame retardancy and mechanical toughness. TG analysis confirms the superior thermal stability and enhanced residue integrity of this composite. In contrast, deviations from this optimal particle size—toward either finer or coarser distributions—result in particle agglomeration or interfacial defects, respectively, which compromise both flame-retardant efficiency and mechanical properties. Supported by SEM and EDS characterization, this work establishes a clear particle size–interface–performance relationship, providing scientific guideline for the precise design of high-performance flame-retardant polyolefins.
However, optimizing the flame retardant efficiency of ATH during practical incorporation remains a subject worthy of in-depth investigation. For instance, variations in ATH particle size lead to differences in its dispersion within the resin matrix, interfacial compatibility, and reaction kinetics, which are critical factors influencing the combustion performance and mechanical properties of composite polyolefins.10,11 Furthermore, controlling the particle size of ATH significantly impacts both the production process and application stability. Large ATH particles tend to settle unevenly in polymer materials, resulting in poor dispersion, while fine particles are prone to agglomeration, making processing difficult and compromising compatibility with the matrix.10,12
Research on foam silicone rubber by Su et al. showed that smaller ATH particles improve mechanical properties like tensile strength but reduce flame retardancy. This non-linear pattern highlights the need to identify an optimal particle size that balances these competing characteristics.13 Shan et al. employed computational modeling to study the flame retardancy of epoxy resin, revealing from a mechanistic perspective that the incorporation of ATH optimizes the material's peak heat release rate, total heat release, and smoke production rate.14
The recent review systematically summarizes the crucial role of microstructure control and interfacial engineering of inorganic fillers (including ATH) in determining the final properties of polymer composites.15 These analyses emphasize that the characteristics of the fillers, such as particle size, distribution, and morphology, are fundamental variables that determine dispersion, interface stress transfer, and thermal–mechanical properties.16,17 This established knowledge system confirms that manipulating the particle structure of ATH is a powerful means for material design.
Although significant progress has been made and the general principles of filler microstructure–property relationships are well-recognized,15,16 a unified and systematic understanding of how ATH particle size characteristics (both median diameter and distribution width) synergistically govern the interfacial properties, thermal decomposition, and fire behavior in highly-filled polyolefin systems specifically designed for LSOH cable sheathing remains conspicuously lacking.10,18–23 In particular, in industrial applications where high load conditions (such as 180 phr) are very common, the optimal balance state remains unclear due to the significant increase in processing and interface-related challenges.
To address the aforementioned issues, this paper selects ATH with different particle sizes as the research subject. Utilizing test methods such as oxygen index, smoke density, and cone calorimetry, it systematically analyzes the combustion behavior of these flame retardants within an LSOH system. Combined with microstructural characterization, the flame retardant mechanism is elucidated, providing a robust theoretical foundation and technical solution for optimizing ATH particle size distribution and developing high-performance, environmentally friendly flame retardant materials.
Precision two-roll mill: Dongguan Zhenggong Electromechanical Equipment Technology Co., Ltd, model ZG-YR-120.
Precision automatic tablet press: Dongguan Zhenggong Electromechanical Equipment Technology Co., Ltd, model ZG-20T.
Flat vulcanizing machine: Huzhou Hongchuan Rubber Machinery Factory, model XLB-D/Q.
Cone calorimeter: FTT (UK), Dual Cone Calorimeter.
Oxygen index analyzer: FTT (UK), Oxygen Index.
NBS smoke density chamber: Mottisco Combustion Technology Instruments (Kunshan) Co., Ltd, model SDB.
UL-94 horizontal and vertical burning test chamber: Shengyuan Systech Co., Ltd, model RH-6033A.
Thermogravimetric analyzer (TGA): Netzsch, model TG 209 F3 Tarsus®.
Scanning electron microscope (SEM): ZEISS (Germany), model Sigma 360.
Universal testing machine: Shanghai Hualong Test Instruments, WDW-0.5C.
Laser particle size analyzer: Dandong Baite Instrument Co., Ltd, BT-9300ST.
Weighed raw materials according to the formulation were melt-blended using a torque rheometer at 140 °C for 15 minutes. The mixture was then sheeted on a two-roll mill at 130 °C. Subsequently, polyolefin sheet materials were obtained through hot pressing (180 °C, 10 min) followed by cold pressing using the flat vulcanizing machine. These sheets were finally cut into test specimens.
Based on the different ATH particle sizes used, the prepared samples were designated as LSOH-1 (ATH median particle size D50 = 1.35 µm), LSOH-2 (D50 = 1.61 µm), LSOH-3 (D50 = 2.28 µm), LSOH-4 (D50 = 2.80 µm), LSOH-5 (D50 = 4.11 µm), LSOH-6 (D50 = 9.82 µm), and LSOH-7 (D50 = 17.77 µm).
| Samples | UL-94 rating (3 mm) | Dripping | LOI/% | |
|---|---|---|---|---|
| Ambient-temp. LOI | High-temp. LOI | |||
| LSOH-1 | V-0 | No | 35.2 | 32.0 |
| LSOH-2 | V-0 | No | 35.7 | 33.2 |
| LSOH-3 | V-0 | No | 37.3 | 34.8 |
| LSOH-4 | V-0 | No | 36.1 | 34.1 |
| LSOH-5 | V-0 | No | 35.3 | 33.0 |
| LSOH-6 | V-0 | No | 31.6 | 29.6 |
| LSOH-7 | V-0 | No | 30.4 | 28.3 |
The aforementioned phenomenon can be attributed to a particle size threshold effect. When the ATH particle size is small, the larger specific surface area promotes good dispersion within the matrix, effectively enhancing flame retardant efficiency. However, when the particle size exceeds a certain threshold, it negatively impacts the oxygen index, likely due to issues such as filler agglomeration and poor dispersion caused by excessively large particles, which adversely affect the material's thermal stability and char-forming ability.19,24 Therefore, during the material design phase, determining the “optimal particle size range” is crucial for ensuring optimized flame retardant performance.
Smoke density testing can objectively quantify the amount of smoke generated by LSOH materials upon exposure to fire, serving as a key indicator for assessing the safety grade of polyolefins.25 Fig. 1 presents the smoke density test results of composite polyolefins with different ATH particle sizes, obtained under the ISO 5659 standard. Under flaming conditions, LSOH-3 exhibited the lowest maximum specific optical density of merely 42.44, demonstrating superior low-smoke characteristics. Under non-flaming conditions, LSOH-1 with the smallest particle size showed the highest smoke density (360.85). As the particle size gradually increased (LSOH-2, LSOH-3, and LSOH-4), the smoke density decreased significantly to approximately 280. However, with further increases in particle size (LSOH-5, LSOH-6, and LSOH-7), the smoke suppression capability of the materials progressively deteriorated.
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| Fig. 1 Smoke density test results of composite polyolefins with different ATH particle sizes under flaming and non-flaming conditions. | ||
ATH with smaller particle size has a larger specific surface area and higher surface energy, which leads to particle agglomeration.26,27 Therefore, uneven and incomplete combustion reactions bring about an increase in the production of smoke. Furthermore, the expanded ATH surface area facilitates more efficient contact with heat and flammable gases, accelerating the decomposition process and generating a large amount of water vapor. The micro “explosion effects” on the surface of polyolefin materials have destroyed the dense protective char layer barrier. The activated alumina obtained by ATH decomposition possesses high surface acidity and catalytic activity, which can catalyze specific pyrolysis reactions, thus generating more small molecule unsaturated hydrocarbons and aromatic compounds, and promoting smoke formation in polymers.28
Conversely, large-particle ATH have poor dispersion and cause defects within the matrix, serving as pathways for smoke and flame penetration, also resulting in substantial smoke production.29
To systematically investigate the impact of aluminum hydroxide (ATH) particle size on the practical fire safety of polyolefin composites, this study evaluated the combustion performance of the materials using a cone calorimeter at the heat flux of 50 kW m−2. By analyzing key parameters such as time to ignition (TTI), peak heat release rate (pHRR), and total heat release (THR) (as presented in Table 2), it was found that the particle size of ATH significantly influences the flame retardancy of the materials.
| Samples | TTI (s) | pHRR (kW m−2) | THR (MJ m−2) |
|---|---|---|---|
| LSOH-1 | 68 | 186.47 | 63.42 |
| LSOH-2 | 72 | 157.27 | 59.26 |
| LSOH-3 | 62 | 129.86 | 56.57 |
| LSOH-4 | 62 | 144.41 | 54.67 |
| LSOH-5 | 60 | 174.20 | 63.68 |
| LSOH-6 | 59 | 189.67 | 67.89 |
| LSOH-7 | 55 | 212.47 | 70.40 |
Fig. 2a shows the heat release rate (HRR) curves of these seven materials. LSOH-3 exhibits a typical bimodal peak structure (“rise-suppression-release” pattern). After ignition, the first heat release peak appears. During this stage, ATH decomposes in an endothermic manner and gradually forms a protective char layer, which inhibits flame spread and causes the HRR to decrease. When the heat accumulates to a certain extent, causing the carbon layer to break or undergo deep decomposition, a second lower-intensity and wider heat release peak will form. The entire HRR curve of LSOH-3 is well-defined and smooth, indicating an orderly and controlled combustion process. In contrast, the HRR curves of other samples show multiple irregular peaks or a jagged, fluctuating pattern, suggesting an unstable combustion process and a lower flame retardant efficiency.
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| Fig. 2 (a) Heat release rate (HRR) curve and (b) fire performance index (FPI) bar chart of ATH composite polyolefin with different particle sizes at the heat flux of 50 kW m−2. | ||
Specifically, when the ATH particle size was 2.28 µm, LSOH-3 exhibited the lowest pHRR (129.86 kW m−2). This represents reductions of approximately 30% and 39% compared to the smallest particle size sample, LSOH-1 (186.47 kW m−2), and the largest particle size sample, LSOH-7 (212.47 kW m−2), respectively. Its performance was also significantly superior to other samples. Furthermore, the THR of LSOH-3 was only 56.57 MJ m−2, indicating a lower total heat release during combustion and suggesting a reduced fire load.
Importantly, to accurately assess the material's “hazard” in a real fire scenario, we specifically calculated the Fire Performance Index (FPI = TTI/pHRR). Generally, the FPI value correlates positively with fire safety; a higher FPI indicates a longer duration from ignition to intense burning, implying higher fire safety.30 As shown in Fig. 2b, the particle size increases progressively from LSOH-1 to LSOH-7. However, the FPI value does not change monotonically with particle size; instead, there is an optimal balance point between combustion performance and particle size (LSOH-3).
In summary, due to the moderate particle size of ATH in LSOH-3, this material achieved the best flame retardant efficiency, attaining an optimal balance between good dispersion and stable decomposition.
Table 3 details the three main mass loss stages and the final residue yield for the seven polyolefin samples containing ATH of different particle sizes during the thermogravimetric test. Preliminary analysis indicates that the flame retardant particle size systematically influences the thermal decomposition behavior of the polyolefins.
| Samples | Tp1 (°C) | R1 (%/min) | Tp2 (°C) | R2 (%/min) | Tp3 (°C) | R3 (%/min) | Residue yield (%) |
|---|---|---|---|---|---|---|---|
| LSOH-1 | — | — | 337.21 | −7.34 | 489.88 | −17.03 | 36.44 |
| LSOH-2 | — | — | 337.77 | −7.92 | 487.73 | −20.88 | 36.76 |
| LSOH-3 | — | — | 334.10 | −7.83 | 492.70 | −19.41 | 37.97 |
| LSOH-4 | — | — | 330.79 | −7.53 | 487.73 | −17.13 | 38.10 |
| LSOH-5 | — | — | 329.40 | −6.97 | 484.48 | −19.56 | 38.71 |
| LSOH-6 | 244.46 | −1.77 | 326.80 | −6.97 | 483.14 | −20.85 | 37.18 |
| LSOH-7 | 242.07 | −1.89 | 322.03 | −6.35 | 486.55 | −21.32 | 37.48 |
Firstly, the first mass loss peak (Tp1) was observed only in LSOH-6 and LSOH-7. This is a negative sign, suggesting that the large ATH particles possess unstable structures, causing premature decomposition of these materials around 240 °C. This prevents their decomposition from cooperating with the decomposition of the polymer matrix, resulting in a decrease in the flame retardant efficiency. This discover correlates well with the higher pHRR and THR values observed for LSOH-6 and LSOH-7 in the cone calorimeter tests. Furthermore, LSOH-7 exhibited the highest mass loss rate in the third stage (absolute value of R3), which also indicates that the large particle components decomposed more intensely at high temperatures, which is not conducive to the impact resistance performance of the material in real fire scenarios. Around 330 °C, the materials produced a second mass loss peak (Tp2), resulting mainly from the overlapping decomposition of the polyolefin matrix and the majority of the ATH. As the particle size increased (from LSOH-2 to LSOH-7), Tp2 showed a linear decreasing trend. This is because smaller particle sizes provide ATH powder with a larger specific surface area, leading to more uniform heat transfer upon heating and thus relatively better thermal stability. The third mass loss peak (Tp3) occurred mainly between 480–490 °C, primarily corresponding to the continued decomposition of ATH, further oxidative decomposition of the char formed from the polymer, or the volatilization of the deep decomposition products of the polymer. LSOH-3 exhibited the highest peak temperature (492.70 °C) for this stage, indicating superior high-temperature stability in the later stages. The residue (char/Al2O3 composite layer) formed by LSOH-3 is the most stable at high temperatures and the most resistant to further oxidative decomposition. The residue yield refers to the proportion of inert substances like aluminum oxide formed after high-temperature decomposition and is often related to the quality of the flame-retardant char.31 LSOH-3 had a residue yield of 37.97%. This favorable residue yield indicates good char-forming ability for this material.
In summary, LSOH-3 demonstrated the best overall performance, exhibiting balanced and stable behavior across the entire temperature range, while simultaneously achieving good high-temperature stability and residue yield.
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| Fig. 4 (a–g) Histograms of particle size distribution and cumulative particle size curves of ATH powders with different particle sizes; (h) SPAN values. | ||
Herein, our work addresses a high-loading (180 phr) polyolefin blend for LSOH cable sheathing. Excessively fine particles (e.g. sub-micron) can lead to severe agglomeration, increased melt viscosity, and poor dispersion, affecting the processing and the formation of a coherent protective char. Therefore, the identified optimum of 2.28 µm, in conjunction with the moderate distribution width (SPAN = 2.19), represents a scenario-specific finding. It demonstrates that for such demanding systems, a moderate micron-scale particle size combined with an optimized distribution is critical for achieving uniform dispersion, strong interfacial adhesion and effective char formation, rather than simply minimizing particle size. This conclusion highlights the significance of tailoring the characteristics (size and distribution) of filler particles based on the specific constraints and performance requirements of the composite material system.
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| Fig. 5 Cryogenically fractured cross-sectional SEM images (a–g) and corresponding EDS maps of Al distribution (insets) for composite polyolefins with different ATH particle sizes. | ||
As the ATH particle size increases (Fig. 5d–g), the particle structure and roughness on the fracture surface of the material become increasingly evident, especially in LSOH-6 and LSOH-7. EDS reveals that the distribution of the Al element presents concentrated, patch-like bright spots, indicating that the ATH has poor dispersion within the matrix and there is a distinct phase boundary. The interfacial adhesion between the large ATH particles and the matrix is weak, which can act as a defect, hindering the formation of carbon and making the flame and heat more likely to penetrate. Furthermore, the internal thermal decomposition of large ATH particles is insufficient, and the synergistic interaction with the polymer matrix is reduced, leading to incomplete and uneven flame-retardant reactions during combustion.
Overall, considering both the microscopic morphology and macroscopic flame retardancy performance, the particle size and dispersion state of ATH are key factors determining the flame retardancy performance of the composite polyolefin. Therefore, in practical applications, selecting ATH with an appropriate particle size and uniform dispersion is crucial for achieving the best flame retardancy performance during combustion.
This can be attributed to the critical role of the filler–matrix interface. A homogeneous microstructure without large agglomerates or voids prevents premature crack initiation, preserving the material's ductility. Conversely, the agglomeration of fine particles (e.g., in LSOH-1, LSOH-2) and the poor adhesion of coarse particles (e.g., in LSOH-5 to LSOH-7) act as stress concentrators, leading to earlier failure and thus lower strength and elongation. Therefore, the optimized ATH particle size (2.28 µm) not only enhances the flame retardancy but also improves the mechanical integrity of the composite material, highlighting its comprehensive applicability in the practical application of LSOH cable sheaths.
The “particle size-interfacial structure-multifunctional performance” correlation model established herein provides a fundamental theoretical framework and a practical approach for designing high-performance halogen-free flame-retardant polyolefins. It demonstrates that by precisely controlling the filler's particulate characteristics, one can concurrently tailor both the fire safety and the mechanical reliability of the composite, which is an essential strategy for developing advanced LSOH cable materials.
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