Open Access Article
Meimei Yu†
ab,
Shuo Qian†ab,
Yuxin Zuo*ab,
Yunya Wuc,
Zhi Li
d,
Zhuo Wange,
Zhiqi Liu
*ab and
Pengfei Chengf
aCollege of Chemistry and Chemical Engineering, Anhui University, Hefei 230601, P. R. China. E-mail: zuoyuxin@ahu.edu.cn; lkeyi@126.com
bInstitute of Future Industry Innovation Research, Anhui University, Hefei 230000, P. R. China
cSchool of Materials Science and Engineering, Anhui University, Hefei 230601, P. R. China
dChina-Spain Collaborative Research Center for Advanced Materials (CSCRC), School of Materials Science and Engineering, Chongqing Jiaotong University, Chongqing 400074, P. R. China
eSchool of Chemical and Process Engineering, University of Leeds, Leeds LS2 9JT, UK
fHefei AnYu He New Materials Technology Co., Ltd, Hefei 230088, P. R. China
First published on 30th March 2026
To address the issue of excessive magnesium aluminum layered double hydroxides (MgAl-LDH) required in ethylene vinyl acetate copolymer (EVA) to achieve effective flame retardancy, which severely impairs the material's mechanical properties, this study explored the synergistic flame retardant effect of ammonium polyphosphate (APP) and MgAl-LDH. A series of EVA blends were prepared via melt blending, with MgAl-LDH as the primary additive and a small amount of APP as the auxiliary flame retardant. The flame-retardant properties, mechanical performance, and char residue characteristics of these blends were systematically evaluated using the limiting oxygen index (LOI) test, UL-94 vertical burning test, cone calorimeter test (CCT), tensile test, and char residue analysis. The results indicated that when the APP content was 8% and the MgAl-LDH content was 47%, the EVA blend achieved a UL-94 V-0 rating, exhibited an LOI value of 29.3%, and demonstrated an elongation at break 52.8% higher than that of the neat EVA (EVA0). This superior performance is primarily attributed to the strong cooperative flame retardant effect of the APP/MgAl-LDH combination, which effectively reduces heat and smoke release during combustion. Furthermore, the incorporation of APP promotes the formation of a dense and continuous char layer on the composite surface, thereby significantly enhancing flame retardant performance. This study is expected to provide a valuable reference for the practical application and green development of flame-retardant EVA materials in the wire and cable industry and construction sector.
The development of halogen-free flame retardant systems with high efficiency, low smoke, low toxicity, and compatibility with material comprehensive properties is thus critical. This has become a key research focus in materials science.7,8 To address traditional flame retardant bottlenecks, researchers have explored multifunctional and cooperative systems. Liang et al.9 developed a chitosan (CS)/phytic acid (PA)/polysilsesquioxane (POSS) wood coating via layer-by-layer self-assembly. It achieved flame retardancy, antibacterial activity, and hydrophobicity through the Si–O–Si barrier and P–N–Si synergy, with a limiting oxygen index (LOI) of 30.9%. Cheng et al.10 prepared ionic liquid-loaded CuO–ZnO hollow microspheres (CZHS@ILs), which synergized with ammonium polyphosphate (APP) to improve epoxy resin (EP) flame retardancy (LOI = 28, UL-94 V-0: peak heat release rate (pHRR) reduced by 74.8%). C. Baoyu et al.11 developed a composite flame retardant composed of ammonium polyphosphate (APP), carbonized foaming agent (CFA), and layered double hydroxides (LDH) containing rare earth elements (La, Ce, Nd) and applied it to EVA matrix. The system improved the flame retardant performance, reaching the V-0 flame retardant grade and significantly reducing the heat and smoke release, and maintained the good mechanical properties of the matrix. Chen et al.12 studied the hydrothermal synthesis of magnesium hydroxide (MH) with hexagonal flake morphology and excellent dispersion. After filling it into EVA matrix, the composite achieved excellent flame retardancy (LOI = 49.2%, UL94 V-0) and significantly improved tensile strength at the same time, with a high filling content of 60wt%. Liu et al.13 compared MgAl LDH prepared with different alkali sources and used it with APP for flame-retardant epoxy resin and obtained LDH with larger layer spacing and higher thermal weight loss. The synergistic effect of MgAl-LDH and APP on the heat release and smoke inhibition of EP was the best.
Traditional halogen-based flame retardants release toxic gases and fumes during combustion, endangering human health and damaging equipment.14–16 Layered double hydroxide (LDH) is a widely used green flame retardant for polymers due to its non-toxic composition.17–19 Kuila et al.20 prepared sodium dodecyl sulfate (SDS)-intercalated LDH (DS-LDH) and synthesized DS-LDH/EVA nanoblends, which showed improved mechanical properties and thermal stability compared to pure EVA. Du et al.21 inserted pentaerythritol diphosphate (PEDP) into LDH and coated it with melamine resin (MF) to obtain D-LDH@MF, a phosphorus–nitrogen clay flame retardant that enhanced EVA thermal stability.
A major drawback of LDH is its high required addition (>60%) for effective flame retardancy in polymers. This high loading impairs mechanical performance due to poor compatibility between inorganic LDH and polymer matrices.22 Surface modification of LDH via physical adsorption or chemical reaction is a common solution to improve dispersion. Y. Feng et al.23 modified magnesium hydroxide (MH) with silanes (KH550, KH570), stearic acid, or titanate and incorporated it into EVA/PE blends, achieving better dispersion and flame retardancy. However, organic modifiers are often flammable, limiting mechanical property improvements and potentially reducing flame retardancy.24
APP is a key halogen-free flame retardant; its thermal decomposition produces ammonia and polymeric phosphoric acid, which shield polymers from oxygen.25,26 Ji27 uniformly dispersed MgAl-LDH and APP in butadiene vinyl rubber/EVA (SBR/EVA) foam cavity walls using epoxy resin and foaming agents. This constructed an insulating layer that reduced initial heat release rate and flammable gas emission. Wang et al.28 prepared microencapsulated APP with melamine–formaldehyde or epoxy resin shells, which significantly enhanced EVA flame retardancy when added alone or with pristine APP.
Recent studies have focused on the flame retardant performance of the APP/LDH combination. It has been confirmed that APP can improve material mechanical properties while reducing heat and smoke emissions.29–31 EVA blends were prepared via melt blending. EVA acted as the polymer matrix, with magnesium–aluminum layered double hydroxide (MgAl-LDH) as the primary flame retardant and ammonium polyphosphate (APP) as the co-flame retardant. The flame retardant and smoke suppression properties of the blends were evaluated using the limiting oxygen index (LOI) test, the cone calorimeter test (CCT), and the vertical burning test. These characterizations aimed to investigate the cooperative flame retardant effect of the MgAl-LDH/APP combination. The optimal mass ratio of MgAl-LDH to APP was determined to maximize flame retardancy through their cooperative interaction. This study provides a feasible strategy for the rational utilization of MgAl-LDH. It also offers a more economical and efficient approach for developing halogen-free flame retardant EVA materials with promising application potential. Additionally, the findings shed new light on the efficient flame retardant modification of LDH-based polymer composites.
| Samples | EVA/wt% | LDH/wt% | APP/wt% | MC226/wt% | LOI/% | UL94 |
|---|---|---|---|---|---|---|
| Pure EVA | 95 | 0 | 0 | 5 | 22.3 | HB |
| EVA0 | 40 | 55 | 0 | 5 | 34.6 | V-0 |
| EVA1 | 40 | 53 | 2 | 5 | 32.6 | V-0 |
| EVA2 | 40 | 51 | 4 | 5 | 30.6 | V-0 |
| EVA3 | 40 | 49 | 6 | 5 | 30.2 | V-0 |
| EVA4 | 40 | 47 | 8 | 5 | 29.3 | V-0 |
| EVA5 | 40 | 45 | 10 | 5 | 28.7 | V-1 |
| Pure APP | 40 | 0 | 55 | 5 | 25.8 | V-0 |
The HB level in UL94 standard is the lowest flame retardant level in the flammability test of plastic materials, that is, there is basically no flame retardant capacity.
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| Fig. 1 Effect of varying APP/LDH ratios on the mechanical properties of EVA blends: (a) elongation at break; (b) tensile strength. | ||
| Samples | T1%/°C | Tmax1/°C | Tmax2/°C | Tmax3/°C | Char yield/% |
|---|---|---|---|---|---|
| Pure EVA | 322.77 | — | 367.18 | 489.14 | 0.11 |
| EVA0 | 230.91 | 297.63 | 399.21 | 491.20 | 30.89 |
| EVA1 | 231.24 | 294.59 | 394.67 | 493.22 | 31.36 |
| EVA2 | 225.72 | 294.09 | 392.53 | 496.81 | 31.61 |
| EVA3 | 217.46 | 286.73 | 386.57 | 497.11 | 31.79 |
| EVA4 | 234.41 | 297.93 | 398.41 | 500.51 | 31.93 |
| EVA5 | 222.19 | 293.73 | 383.03 | 499.53 | 32.92 |
| Pure APP | 338.83 | — | 353.64 | 469.49 | 30.41 |
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| Fig. 2 Thermal degradation behavior under N2 atmosphere: (a) TGA and (b) DTG curves of EVA blends with varying APP/LDH ratios. | ||
As illustrated in Fig. 2(a), neat EVA initiates thermal degradation at 322.77 °C and undergoes a two-stage decomposition process. The first decomposition stage occurs at 367.18 °C, which is attributed to the cleavage of carboxylic acid groups, while the second stage takes place at 489.14 °C, corresponding to the breakdown of ethylene backbone chains. Notably, the char residue of neat EVA at elevated temperatures (up to 800 °C) is nearly negligible. In order to understand the role of LDH in composites, the thermal behavior of LDH was analyzed. As shown in Fig. 2, the TGA-DTG curve of MgAl-LDH shows typical multi-stage decomposition characteristics. The initial weight loss temperature (T1%) is 230.91 °C, which corresponds to the removal of physical adsorption water and part of interlayer water. In the first stage, the maximum weight loss peak (Tmax1) appeared at 297.63 °C, mainly due to the hydroxyl removal of the laminate. The second stage maximum weight loss peak (Tmax2) is located at about 399.21 °C, which is related to the decomposition of interlayer carbonate ions and further structural dehydration. In some tests, the third stage of weight loss (Tmax3) can be observed at 491.2 °C, representing the complete conversion to mixed metal oxides (MgO, Al2O3). After high temperature of 800 °C, the char yield of pure LDH reached 30.89%, which was mainly due to the thermal stable metal oxides formed by its decomposition.
With the incorporation of LDH into the EVA matrix, the initial decomposition temperature (IDT) of the composite decreases to 230.91 °C, which is substantially lower than that of neat EVA. This phenomenon arises from the abundant interlayer water and hydroxyl (–OH) groups in the LDH structure, which release structural water (H2O) and carbon dioxide (CO2) at relatively low temperatures, thereby triggering the premature thermal decomposition of the EVA matrix. Despite lowering the IDT, the release of these non-combustible gases dilutes the concentration of flammable volatiles, thus exerting a gas-phase flame-retardant effect. The char residue of the EVA0 composite at 800 °C increases to 30.89%, endowing the material with inherent flame-retardant properties. Furthermore, the char residue rates of EVA ternary blends containing both APP and LDH are higher than those of EVA0. This enhancement stems from the thermal decomposition of APP to form polyphosphoric acid, which catalyzes the dehydration and cross-linking of the EVA matrix to generate an intumescent char layer. Concurrently, LDH decomposes to produce metal oxides (MgO, Al2O3), which react with polyphosphoric acid to form thermally stable metal phosphates. These phosphates reinforce the mechanical strength and thermal stability of the char layer. Synergistically, APP and LDH cooperate to construct a dense, continuous composite protective barrier, which effectively isolates heat and oxygen penetration while suppressing the release of flammable volatiles. This synergistic effect elevates the char residue rate, highlighting the prominent condensed-phase flame-retardant efficiency of the hybrid system. This finding further corroborates the existence of a distinct synergistic flame-retardant interaction between APP and LDH.33
As shown in Fig. 2(a), the EVA composite undergoes a three-stage weight loss process during TGA testing. The initial weight loss stage is associated with the evaporation of weakly bound interlayer water from the LDH component within the composite. The subsequent two decomposition stages involve dehydroxylation and decarbonylation reactions in the LDH crystal lattice, along with the cleavage of acetic acid groups in the EVA side chains and the fragmentation of the EVA main chain. Moreover, EVA0 exhibits a faster decomposition rate than neat EVA in the first two stages, whereas its decomposition rate slows down in the third stage. This trend is ascribed to the accelerated cleavage of carboxylic acid groups induced by LDH, which, in turn, reduces the decomposition rate during the final stage of thermal degradation.34
The derivative thermogravimetry (DTG) curves presented in Fig. 2(b) provide further insight into the degradation kinetics and the synergistic effect between APP and LDH. For the LDH-filled composite (EVA0), three distinct peaks corresponding to the aforementioned stages are observed at 297.63, 399.21, and 491.20 °C, respectively. The first peak is attributed to the loss of interlayer water from LDH, while the second and third peaks correspond to the deacetylation of EVA and the main-chain scission, overlapping with LDH dehydroxylation.
Remarkably, the addition of APP significantly alters the DTG profile. As shown in Fig. 2(b), with increasing APP content (e.g., from EVA1 to EVA5), the second decomposition peak (Tmax2, associated with EVA deacetylation) shifts to lower temperatures initially, then stabilizes or slightly increases for optimal formulations (e.g., 398.41 °C for EVA4). More importantly, the third decomposition peak (Tmax3, representing the most thermally stable component and the integrity of the char layer) shows a consistent and notable shift to higher temperatures. As listed in Table 2, the final-stage decomposition temperature (Tmax3) of the optimal composite EVA4 (500.51 °C) is not only 9.3 °C higher than that of the LDH-only composite EVA0 (491.20 °C) but also substantially exceeds that of the APP-only sample (469.49 °C). This consistent increase in Tmax3 for the blends, surpassing both individual components, strongly indicates the formation of a more thermally stable char residue due to the interaction between APP-derived phosphoric acids and LDH-derived metal oxides. Similarly, the char residue at 800 °C for EVA4 (31.93%) is higher than that of EVA0 (30.89%), suggesting that APP enhances the char-forming efficiency of the LDH system, rather than simply providing an additive effect. The TGA and derivative thermogravimetry (DTG) curves of LDH, APP, and the resultant composites (EVA4) are provided in Fig. S3.
T1% represents the temperature at 1% mass loss. Tmax1, Tmax2, and Tmax3 correspond to the temperatures of the maximum mass loss rate in the first, second, and third decomposition stages, respectively.
During combustion, the incorporation of APP into the EVA composite facilitates the cross-linking of the polymer matrix and promotes its carbonization. This subsequently induces the formation of a dense, intact char layer on the material surface. Serving as an efficient thermal barrier, the char layer effectively shields the underlying polymer matrix, thereby reducing the pyrolysis rate and suppressing the generation of flammable volatiles.37
Fig. 3 presents the heat release rate (HRR) and total heat release (THR) profiles of neat EVA and EVA blends with different APP/LDH ratios. As shown in Fig. 3(a), neat EVA exhibited a peak HRR (pHRR) of 862.9 kW m−2 at 110 s, with complete combustion occurring at 187 s. The unimodal HRR profile of neat EVA is indicative of combustion without char formation. For the EVA composite with LDH added alone, the HRR decreased significantly and exhibited a bimodal distribution. The first peak (250.9 kW m−2) emerged at 115 s, corresponding to the initial combustion of the polymer matrix. In contrast, the second peak (209.7 kW m−2) at 300 s was attributed to the cracking of the fragile char layer under sustained thermal exposure. With the incorporation of APP to adjust the APP/LDH ratios, the HRR curves of EVA blends also displayed bimodal characteristics: the first peak appeared earlier than that of the LDH-only composite, while the second peak was delayed. This phenomenon confirms that APP addition catalyzes the formation of a robust, dense char layer, which more effectively blocks the diffusion of flammable volatiles into the combustion zone. As illustrated in Fig. 3(b), the THR of EVA blends at 300 s decreased from 60.56 MJ m−2 (neat EVA) to 44.96 MJ m−2 (EVA0) and was further reduced to 31.90 MJ m−2 with 8 wt% APP loading. The introduction of APP thus further lowered the HRR and effectively diminished the total heat output of EVA blends throughout the combustion process. The reduction in THR values demonstrates a distinct synergistic flame-retardant effect between APP and LDH, which significantly enhances the fire resistance of EVA blends and yields a superior flame-retardant performance.
Fig. 3 also depicts the smoke production rate (SPR) and total smoke production (TSP) curves of neat EVA and EVA blends with different APP/LDH ratios during combustion. As shown in Fig. 3(c), neat EVA exhibited rapid and extensive smoke release after ignition, with a peak SPR of 0.112 m2 s−1 at 105 s. The EVA composite containing only LDH reached a maximum SPR of 0.044 m2 s−1 at 285 s. With the gradual incorporation of APP (the proportion of LDH decreases accordingly), the SPR curves of EVA blends also showed bimodal behavior. The first peak originated from smoke generated during the initial combustion of the polymer matrix, while the second peak was caused by the cracking of the char layer, which was insufficiently robust to withstand prolonged burning, after APP-induced carbonization. The first SPR peak appeared at 90 s, which was associated with the surface combustion of the material; this earlier onset indicates that APP accelerates the charring process of the EVA matrix. Compared with LDH, APP acts as both a charring catalyst and a char-layer reinforcer, resulting in the second SPR peak occurring later and with lower intensity after material combustion. The second SPR peak of the APP-containing blends emerged at approximately 415 s, with a maximum value of 0.0088 m2 s−1; this was attributed to the enhanced thermal stability of the char layer formed during combustion. As shown in Fig. 3(d), the TSP of EVA composites at 300 s decreased from 8.59 m2 (neat EVA) to 6.24 m2 (EVA0) and was further reduced to 4.26 m2 with 8 wt% APP loading. This result highlights the role of APP in accelerating the early-stage degradation of the polymer matrix and promoting the formation of a continuous, dense char layer, thereby effectively suppressing smoke emission during combustion.40
In Table 3, the time to ignition (TTI) of all EVA composites is significantly longer than that of pure EVA. Among them, the TTI of EVA0 is the longest, which is attributed to the delayed effect of endothermic LDH decomposition and gas dilution on ignition. After adding APP, TTI was shortened, which was because while APP promoted the early degradation and charring reaction, it also helped to form a protective carbon layer earlier in the process, thus changing the combustion process. Fire growth rate index (FIGRA: ratio of peak heat release rate pHRR to time to peak) is a key index for assessing fire risk. All samples containing flame retardant FIGRA (2.18–2.97 kW [m2 s]−1) were far lower than pure EVA (7.84 kW [m2 s]−1). The FIGRA of EVA4 is 2.77 kW [m2 s]−1, which is at a low level, indicating that its fire risk is significantly reduced and its combustion growth is slow. The residual carbon rate directly reflects the flame retardant effect of the condensed phase. With the partial substitution of APP for LDH, the carbon residue rate of the composite increased from 11.68% for EVA0 to 13.97% for EVA5. This directly confirms the synergy of APP and LDH in promoting carbon formation: APP catalyzes the formation of a carbon layer, while LDH decomposition products enhance the carbon layer, leading to more stable carbon residue.
| Samples | TTI (s) | pHRR (kW m−2) | pSPR (m2 s−1) | THR (MJ m−2) at 300 s | TSP (m2) at 300 s | FIGRA (kW [m2 s]−1) | Char yield (%) |
|---|---|---|---|---|---|---|---|
| a Char yield is the residual mass percentage at 800 °C. | |||||||
| Pure EVA | 31 | 862.9 | 0.112 | 60.56 | 8.59 | 7.84 | 0 |
| EVA0 | 64 | 250.9 | 0.044 | 44.96 | 6.24 | 2.18 | 11.68 |
| EVA1 | 47 | 243.6 | 0.025 | 39.36 | 5.30 | 2.87 | 12.98 |
| EVA2 | 45 | 232.3 | 0.029 | 35.64 | 4.73 | 2.73 | 13.69 |
| EVA3 | 45 | 237.6 | 0.029 | 36.70 | 4.20 | 2.97 | 13.58 |
| EVA4 | 47 | 221.9 | 0.029 | 31.90 | 4.26 | 2.77 | 13.57 |
| EVA5 | 45 | 222.3 | 0.027 | 32.87 | 4.13 | 2.78 | 13.97 |
| Pure APP | 43 | 414.4 | 0.035 | 72.95 | 5.99 | 1.78 | 65.84 |
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| Fig. 4 SEM and digital photographs of the residues after cone calorimetry tests for (A-0) pure EVA, (B-5) EVA0, (E-2) EVA3, and (E-4) EVA5. | ||
The synergistic flame-retardant mechanism of APP and Mg–Al layered double hydroxide (Mg–Al-LDH) is elucidated as follows. First, condensed-phase synergy serves as the core mechanism, which enhances catalytic char formation: polyphosphoric acid derived from the thermal decomposition of APP catalyzes the dehydration and cross-linking of the polymer matrix to form an intumescent char layer. Meanwhile, metal oxides (MgO, Al2O3) generated by the thermal decomposition of Mg–Al-LDH react with polyphosphoric acid to form thermally stable metal phosphates. These phosphates contribute to the construction of a robust, dense, and continuous composite protective barrier that effectively blocks heat and oxygen transfer to the underlying polymer matrix and inhibits the release of flammable volatiles. Second, gas-phase synergy complements the condensed-phase effect: the decomposition of Mg–Al-LDH releases water vapor (H2O) and carbon dioxide (CO2), which dilute the concentrations of oxygen and flammable gases in the combustion zone, thereby interrupting the combustion chain reaction. Concurrently, the thermal decomposition of APP is an endothermic process that absorbs substantial heat. It also releases ammonia (NH3) and other non-combustible gases, which further enhance the gas-phase dilution effect. Collectively, the endothermic decomposition processes of APP and Mg–Al-LDH absorb significant heat, effectively cooling the polymer matrix and decelerating its pyrolysis rate.42,43
Fig. 5 shows the XRD patterns of the char residues from pure EVA and EVA blends with varying APP additions after CCT. The XRD patterns reveal distinct peaks corresponding to crystalline phases formed during combustion. For pure EVA, the absence of significant crystalline peaks indicates that the material burns completely without forming a stable char layer. In contrast, the EVA0 sample (containing 55% LDH) exhibits peaks characteristic of metal oxides, which are decomposition products of LDH. These metal oxides contribute to the formation of a residual char layer, albeit with limited structural integrity, as evidenced by minor cracking observed in the digital photographs (Fig. 4).
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| Fig. 5 XRD patterns of the char residues from EVA blends with different APP/LDH ratios after cone calorimetry tests. | ||
With the incorporation of APP, the XRD patterns of the blends (EVA1 to EVA5) show additional peaks corresponding to metal phosphates. These compounds are formed through reactions between polyphosphoric acid (released from APP decomposition) and metal oxides (from LDH decomposition). The presence of metal phosphates enhances the thermal stability and mechanical strength of the char layer, leading to a denser and more continuous protective barrier. This is consistent with the observed improvements in flame retardancy, such as reduced heat release rate (HRR) and smoke production (Fig. 3).
In contrast to pure EVA and EVA0, the incorporation of APP significantly altered the morphology and composition of the char residue. To further elucidate these changes, the XRD pattern of the optimal EVA4 blend (47 wt% LDH, 8 wt% APP) is examined in detail (Fig. 5). It shows distinct crystalline diffraction peaks at approximately 2θ = 43.0°, 62.5°, and 78.7°, which can be indexed to the (200), (220), and (222) crystal planes of cubic periclase-structured magnesium oxide (MgO, ICDD PDF card no. 79-0612). This confirms that during combustion, the MgAl-LDH additive underwent thermal decomposition, ultimately forming crystalline MgO as a stable solid residue within the char layer. The presence of such well-defined, crystalline metal oxides significantly contributes to the mechanical strength and thermal stability of the protective char barrier.44 The formation of crystalline MgO is a key outcome of the cooperative flame-retardant mechanism. The metal oxides (MgO and Al2O3) derived from LDH decomposition can react with polyphosphoric acid (generated from APP thermal decomposition) to form thermally stable metal phosphates.45 While the characteristic peaks of such phosphates or Al-containing phases might overlap or be less intense in the patterns of EVA1 to EVA5, the prominent MgO peaks in EVA4 provide direct evidence of the condensed-phase actions of LDH and its synergistic interaction with APP in reinforcing the char structure.
The intensity of the carbon-related peaks in the XRD patterns increases with higher APP content, indicating enhanced carbonization and cross-linking within the char layer. This aligns with the conclusions drawn from the digital photographs (Fig. 4), where the char layer coverage expands with increasing APP addition. The synergistic interaction between APP and MgAl-LDH promotes the formation of a composite protective layer comprising carbon, metal oxides, and metal phosphates, which effectively isolates the polymer matrix from external heat and oxygen.
Supplementary information (SI): Fig. S1: The FTIR of LDH, APP, and compound; Fig. S2: The SEM of (a) LDH, (b) APP, and (c) compound; Fig. S3: (a) TGA and (b) DTG curves of LDH, APP, and compound; Fig. S4: the particle size of Mg–Al-LDH; Fig. S5: XRD patterns of pure EVA and pure APP; Table S1: variance report of tensile test results. See DOI: https://doi.org/10.1039/d6ra00909c.
Footnote |
| † These authors contributed equally to this work. |
| This journal is © The Royal Society of Chemistry 2026 |