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Review Article
ARTICLE IN PRESS
doi:
10.25259/AJC_1269_2025

Research on the characteristics of montmorillonite microcapsule inhibitors for suppressing coal dust explosion

College of Safety Science and Engineering, Liaoning Technical University, Huludao, Liaoning, China
Key Laboratory of Mine Thermo-motive Disaster and Prevention, Ministry of Education, Huludao, Liaoning, China
College of Power Engineering, Bohai Shipbuilding Vocational College, Huludao, Liaoning, China

*Corresponding authors: E-mail addresses: gaoke@lntu.edu.cn (K. Gao) and chenlulntu@163.com (L.Chen)

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Abstract

To minimize the substantial amount of highly explosive flammable dust and coal dust present in coal mine working faces, relatively effective suppression measures have been adopted. Na-MMT@CS@PA-Na, a core-shell structural blast inhibitor, was experimentally synthesized using sodium-based montmorillonite (Na-MMT) with pore structure as the carrier and chitosan (CS) and sodium phytate (PA-Na) as the active components was used to analyze the physical and chemical properties of coal dust. The results showed that the synergistic effect of Na-MMT@CS@PA-Na eliminated the bright burning area of the flame, with the flame propagation speed being lower than the average speed of 1.469 m/s, and the peak temperature being limited to 89°C. The pressure parameters showed substantial reductions, reducing maximum overpressure (Pmax) by 92.9% and maximum pressure rise rate (dP/dtmax) by 94.6%, far exceeding the performance of individual component materials. At interring ratios (α=0.045), a negative oscillation in the flame speed occurred, and it had significant inhibitory effects on both temperature and pressure. Conversely, individual PA-Na and Na-MMT only weakly reduced flame brightness or created non-luminous zones. The scanning electron microscopy (SEM) and X-ray photoelectron spectroscopy (XPS) analyses reveal the physical suppression mechanism. Among them, Na-MMT@CS@PA-Na significantly reduces the explosion effect in multiple aspects. Its inhibitory effect is superior to that of Na-MMT and PA-Na, and the optimal inertization rate α=0.045. This study has achieved important experimental basis and theoretical reference for the flame propagation behavior of coal dust explosion in enclosed pipelines using new microcapsule materials.

Keywords

Coal dust explosion
Element valence state
Flame propagation
Microcapsules
Montmorillonite

1. Introduction

Coal dust explosion, as a major safety hazard in coal mines, generates shockwaves that not only directly damage roadway facilities but also stir up deposited coal dust, triggering secondary explosions with greater destructive power, which seriously threaten the lives and property safety of underground workers. This poses a serious threat to both personnel safety and property security in underground operations. Under deep mining conditions, the risk of coal dust explosions increases rapidly with higher coal seam gas content and intensified mining activities. Traditional passive prevention measures such as water mist spraying and ventilation dilution have become inadequate in addressing instantaneous explosions of high-concentration coal dust. Consequently, the development of efficient and environmentally friendly composite explosion suppressants has emerged as a critical breakthrough in enhancing mine safety standards. This advancement holds significant strategic importance for establishing proactive prevention systems and ensuring safe energy production.

Explosion suppression technology represents one of the principal methodologies in the field of explosion prevention and control, with its efficacy contingent upon the performance characteristics of suppression materials [1,2]. In recent years, researchers have systematically investigated the macroscopic patterns of inert gases, fine water mist, chemical powders, and halocarbons in suppressing gas explosions [3-5], accompanied by in-depth theoretical analyses of their mechanisms. Inert gases function by reducing the concentration of combustible gases or dust in the environment, thereby preventing explosive mixtures from reaching combustion conditions. Fine water mist suppresses gas explosions through both physical and chemical pathways. Chemical powders such as CaCO3 and NH4H2PO4 exert suppression effects through multiple mechanisms. Certain halocarbon gases exhibit dual characteristics of both promoting and inhibiting gas explosions, yielding significant phased achievements. Zhang et al. [6] developed a novel dry powder fire extinguishing agent CSFP-ATH, with experimental results demonstrating that smaller particle sizes and larger specific surface areas correspond to enhanced fire suppression capabilities, while Al(OH)3 manifests both physical and chemical inhibition effects. Wu et al. [7] investigated the mitigation of coal dust explosion hazards using a novel silica (SiO2) aerogel synthesized from diatomite. Experimental results demonstrate that the newly developed SiO2 aerogel effectively retards the aerosolization and oxidation processes of coal dust. Zhang et al. [8] confirmed that the composite powder CuO-CeO2/CaO, while utilizing its catalytic adsorption properties to eliminate CO and CO2, reduces gas explosion pressure through chain reaction interruption, dilution asphyxiation, and endothermic adsorption of products. Raza et al. [9,10] synthesized highly porous cubic crystal MoO3 (α-MoO3) nanosheet-like structures on nickel foam (Ni-F) using the chemical vapor deposition (CVD) technique. The results showed that the excellent electrochemical properties of α-MoO3 make it suitable as an electrode material for supercapacitor applications. Iqbal et al. [11] enhanced the performance of supercapacitors by synthesizing NiO and Ce-NiO nano-plates-based electrodes to increase its specific surface area and pseudocapacitive contribution, while significantly reducing the optical band gap, rendering it suitable for applications in solar cells and energy storage devices. Ibrahim et al. [12]. Studied the preparation of CoTe2 electrode using the hydrothermal method, and their supercapacitive performance was excellent. The assembled device had an energy density of 280Wh/kg, and also exhibited good non-enzymatic glucose sensing activity. Yang [13] employed a dissolution crystallization method to load KHCO3 onto diatomite surfaces, compensating for KHCO3 limited adsorption sites and small specific surface area, thereby enabling the composite suppression agent to fully leverage its physicochemical synergistic inhibition effects. Yan et al. [14] developed a microencapsulated ammonium phosphate explosive suppressant with a core-shell structure, which exhibits inhibitory effects on the explosion and combustion of various metamorphic coals. This formulation effectively controls flame propagation and pressure rise during coal dust explosions.

Research on montmorillonite predominantly focuses on its application in composite inhibitors formed with other compounds [15,16], and the effectiveness of its implementation in practical engineering. Zhang et al. [17] utilized a novel Gemini surfactant, hexadecyl dimethyl ammonium chloride, to modify sodium montmorillonite for phenol adsorption in simulated wastewater. Wang et al. [18] validated the superior explosion-proof performance of calcined montmorillonite powder in suppressing shock waves and flame propagation in pipeline networks during methane explosions. Mi et al. [19] studied the surface properties of montmorillonite and found that the surface adsorption had different effects on the growth of carbon dioxide hydrates and the methane-carbon dioxide exchange. Wang et al. [20] investigated the explosion suppression performance of carbon dioxide-driven calcified montmorillonite powders with varying particle sizes. The results indicate that the optimal suppression effect is achieved when the powder particle size ranges from 21 to 32 micrometers. Ning et al. [21] studied the adsorption efficiency of three minerals for BDOM, with the formation efficiency of mineral-bound organic matter ranked as montmorillonite > hematite > quartz sand, where montmorillonite’s superior BDOM adsorption is attributed to its larger specific surface area providing more adsorption sites and more pronounced cation bridging effects. Mi et al. [22] explored multiple mechanisms by which montmorillonite or reservoir clay promotes CO2 and H2 generation during crude oil cracking, including acid catalysis, adsorption of oxygen-containing organic matter cracking, and hydration of interlayer water with organic matter. Li et al. [23] developed a functional separator modified with MnO2 -coated montmorillonite (MnO2-MMT-PP). The study demonstrates that the montmorillonite (MMT) substrate not only enhances the transport efficiency of lithium-ion batteries but also serves as a structural framework, facilitating the uniform dispersion of MnO2 nanoparticles and thereby generating a synergistic effect. Chen et al. [24] used MMT, melamine cyanurate (MCA), and diethyl phosphate aluminum (ADP) as raw materials to prepare a nitrogen-phosphorus-silicon synergistic explosion inhibitor (MCA@ADP-MMT). They also studied the inhibitory effect and mechanism of this inhibitor. The experiments showed that there was a strong correlation between the inhibitory effect of MCA@ADP-MMT and the inhibitor concentration. At high concentrations, it effectively alleviated the explosion of aluminum powder. Although numerous studies have confirmed that MMT has an inhibitory effect on explosions, the mechanism of the inhibitory effect of montmorillonite on coal dust explosions is still not fully understood at present.

This study selected multiple components including chitosan (CS), sodium phytate (PA-Na), absolute ethanol, and anhydrous acetic acid as raw materials. Following a specified preparation protocol, the microcapsule material Na-MMT@CS@PA-Na was synthesized. The material was characterized using scanning electron microscopy (SEM) and X-ray diffraction (XRD) techniques. Fourier-transform infrared spectroscopy (FTIR) was employed to analyze the functional groups of the material. Additionally, thermogravimetric analysis (TG) and differential scanning calorimetry (DSC) were conducted to investigate the decomposition behavior of the Na-MMT@CS@PA-Na microcapsule powder, leading to the proposal of the mechanism of action for the explosion inhibitor. Within a self-constructed coal dust explosion suppression test system, the explosion characteristics of 200-mesh lignite coal dust at a concentration of 250 g/m3 were studied under different explosion inhibitors (Na-MMT, PA-Na, Na-MMT@CS, Na-MMT@CS@PA-Na) and various inserting ratios (α = 0, 0.015, 0.030, 0.045). The study explored the patterns of explosion suppression effectiveness at different inhibitor concentrations and comprehensively analyzed the performance of the microcapsule inhibitor and its components. The findings indicate that the Na-MMT@CS@PA-Na explosion inhibitor exhibits significantly superior suppression effects compared to single-component inhibitors.

2. Materials and Methods

2.1. Experimental scheme

2.1.1. Experimental setup

This paper presents the development of a coal dust explosion suppression agent, Na-MMT@CS@PA-Na, based on independent research and tested using self-built explosion suppression system, as illustrated in Figure 1. The experimental apparatus comprises several core components, including a vertical combustion tube, powder injection system, ignition system, synchronous control unit, image acquisition system, sensors, and an oscilloscope.

Schematic diagram of experimental setup.
Figure 1.
Schematic diagram of experimental setup.

The vertical combustion tube used in the experiment consists of a steel body, quartz glass, a top cover, and sealing screws, exhibiting excellent sealing performance. The external dimensions are 140 m×140 mm×500 mm, while the internal dimensions are 90 mm×90 mm×475 mm, with a volume of 3.8 L and a rated pressure resistance of 3.0 MPa. The front section of the tube is made of transparent, high-temperature-resistant quartz glass (pressure-resistant up to 2 MPa), measuring 60 mm×300 mm with a glass wall thickness of 280 mm. The powder spraying system, controlled by a controller, injects compressed air into the powder reservoir at 2 MPa to maintain constant pressure inside the explosion chamber after spraying. The ignition system uses electric pulse ignition, with a single electrode tube with a length of 42 mm and an electrode spacing of 6 mm. The ignition position is approximately 100 millimeters above the bottom of the combustion tube. It generates a 60J electric spark. The image acquisition system captures the explosion flame structure, with a high-speed camera set at 807 fps, operating for 4 s at a resolution of 2048×1536. Thermocouples and pressure sensors are mounted on the right side of the combustion tube. Temperature is measured using a Pt13% Rh-Pt precision thermocouple, 100μm in diameter, with a range of 0°C to 800°C. The PCB 113B21 pressure sensor features a range of 1379 kPa, sensitivity of ±15% (or 3.6 mV/kPa), and a weight of 6 g. The oscilloscope YOKOGAWA DL950 records temperature and pressure variations. The CH1 and CH3 modules were chosen for pressure and temperature measurement respectively, with a response time of 0.02ms, a sampling rate of 15kHz, and the trigger mode set to automatic triggering of the CH3 temperature module at 25°C and the running time was 5 s. The trigger position was set at 30% of the screen. After each explosion experiment, samples of the residual particles in the pipeline were collected, and the experiment was repeated three times under each operating condition.

The experiments are categorized into two types: empty explosion tests and inhibitor-coal dust composite explosion tests. In the absence of any anti-explosion agent, coal dust explosion tests were conducted to measure parameters such as maximum explosion pressure, serving as a control group. Each group underwent 3-5 parallel trials, with the average value taken. Subsequently, coal dust was uniformly mixed with the anti-explosion agent, and explosion tests were conducted at different inserting ratios. The explosion characteristic curves were analyzed, the maximum explosion pressure was calculated, and the interaction mechanism between microcapsule anti-explosion agents and coal dust was explored.

2.1.2. Selection of experimental coal dust

The experimental coal samples used in this study were collected from Pingzhuang Coal Mine in Chifeng City, Zerim League, Inner Mongolia. This coal mine has an excellent geographical location, with coordinates of 42.069°N and 119.219°E. Pingzhuang Coal Mine is renowned for its abundant production of lignite, and its coal quality is unique, with a carbon content ranging from 60% to 77%, heat value approximately 23.0-27.2 megajoules per kilogram (equivalent to 5500-6500 kilocalories per kilogram), density about 1.1-1.2 g/cm3, and volatile matter exceeding 40%. The coal samples are mostly brown or dark brown in color, with a relative density ranging from 1.2 to 1.45, making them ideal materials for studying the characteristics of coal dust explosions.

The particle size characteristics of coal dust were analyzed using SEM. The particle size distribution of the coal sample was measured using a Malvern Mastersizer 2000 in accordance with international standards, with detailed data illustrated in Figure 2. The experimental coal sample contained 90% of particles smaller than 47.38 μm, 50% smaller than 13.58 μm, and 10% smaller than 2.55 μm, satisfying the explosive conditions.

Particle size analysis of coal dust.
Figure 2.
Particle size analysis of coal dust.

2.2. Preparation of microencapsulated materials

In this experiment, CS [25], PA-Na, anhydrous ethanol and anhydrous acetic acid were used as experimental materials, all of which met the AR standard [26,27].

The Na-MMT@CS composite was first prepared. Precisely 2 g of CS was weighed and gradually dissolved in 200 mL of a 2 wt% aqueous acetic acid, with continuous stirring until the pH was adjusted to 5. Then, 2 g of Na-MMT was slowly added to the CS solution and stirred vigorously to ensure uniform dispersion. After 2 h, the suspension was transferred to centrifuge tubes and centrifuged at 3500 rpm for 5 minutes to achieve solid-liquid separation. The collected solid mixture was washed with deionized water to remove residual ions, followed by two washes with anhydrous ethanol to reduce moisture content. The washed solid was dried in a oven at 70°C for 12 h, and then ground into a powder to obtain the final product, labeled Na-MMT@CS.

Subsequently, the Na-MMT@CS@PA-Na microcapsule was prepared. Exactly 2 g of sodium phytate (PA-Na) was dissolved in 200 mL of deionized water (DW) and stirred mechanically for 30 minutes to form a PA-Na suspension. Concurrently, an appropriate amount of Na-MMT@CS was uniformly dispersed in DW and stirred mechanically for 30 minutes. The PA-Na suspension was slowly added dropwise to the Na-MMT@CS suspension under continuous stirring at room temperature (RT) for 2 h to ensure complete reaction. After the reaction, the mixture was centrifuged at 3500 rpm for 5 minutes. The supernatant was discarded, and the solid was washed twice with DW and twice with anhydrous ethanol. The washed product was dried at 70°C for 12 h, then ground into powder to obtain the final microcapsule product.

2.3. Characterization of microcapsule materials

2.3.1. Macroscopic morphology

SEM was used to obtain microscopic images of microcapsule explosion agents and their raw materials at magnifications of 500 times, 1000 times, and 5000 times. Figure 3(a) shows the SEM images of CS, Na-MMT, PA-Na, Na-MMT@CS, and Na-MMT@CS@PA-Na. The unmodified Na-MMT displays a typical loosely structured layered silicate, in which amorphous sheets overlap due to van der Waals forces and uneven surface charges, forming a porous network. The particle sizes vary greatly, and the thickness distribution is non-uniform. This cross-fiber structure results from electrostatic equilibrium between interlayer cations and the negative charges of silicon-oxygen tetrahedra, maintaining open interlayer channels and preventing particle aggregation.

(a) Surface morphology of CS, PA-Na, Na-MMT, Na-MMT@CS and Na-MMT@CS@PA-Na. (b) Elemental mapping images of Na-MMT@CS@PA-Na.
Figure 3.
(a) Surface morphology of CS, PA-Na, Na-MMT, Na-MMT@CS and Na-MMT@CS@PA-Na. (b) Elemental mapping images of Na-MMT@CS@PA-Na.

CS exhibits the granular morphology of polysaccharide polymers, with nearly spherical individual particles. However, due to the hydrogen bonding network formed by surface hydroxyl groups, the particles tend to aggregate into chain-like or cluster-like structures. PA-Na exhibits a hierarchical porous structure with a dense surface and uneven particle sizes, often agglomerating into clusters. This loose and porous structure is attributed to the steric hindrance of phytic acid ions. Both CS and PA-Na clearly show agglomeration tendencies, providing morphological conditions for subsequent observations of adsorption and encapsulation on the Na-MMT surface.

Compared to unmodified Na-MMT, Na-MMT@CS fibers exhibit stronger interfacial bonding. Irregular CS particles adhere to Na-MMT, resulting in shortened and thickened rod-like structure and the formation of a surface film. Additionally, Na-MMT@CS@PA-Na particles show well-defined contours, rough surfaces, and uniform coverage with numerous aggregates. This indicates the formation of a new “skin” layer on the Na-MMT@CS surface, confirming the successful synthesis of the microcapsule structure.

Figure 3(b) shows the EDX elemental mapping results of the Na-MMT@CS@PA-Na microcapsule material. Six elements, C, O, Na, Mg, Al, Si, are clearly marked in different colors, with mass percentages of 14.84%, 29.75%, 0.63%, 0.43%, 2.1%, and 52.25%, respectively. As shown in Table 1, the C and O elements are widely and uniformly distributed, which aligns with the expected distribution pattern of organic components in CS and PA-Na. Unlike the uniformly distributed organic elements, inorganic elements such as Na, Mg, Al, and Si exhibit significant localized enrichment, which reflects the typical layered structure of Na-MMT.

Table 1. Na-MMT@CS@PA-Na distribution of elements.
Element C O Si Na Mg Al
Wt% 14.84 29.75 52.25 0.63 0.43 2.10
At% 24.32 36.62 36.63 0.54 0.35 1.54

2.3.2. Crystal structure analysis

The material’s crystal structure was analyzed using XRD. The XRD pattern of the sample is shown in Figure 4(a). The broad peak at 2θ=19.9° corresponds to the crystalline structure of the polymer CS [28,29]. For MMT, diffraction peaks at 2θ=6.7, 14.2, 19.7, 28.7, 34.7, 40.3, 43.4, 53.0, and 61.8 are consistent with the peak positions of natural MMT. The XRD pattern of MMT@CS shows that montmorillonite partially decomposes in the acidic CS solution. The intensity of its characteristic peaks slightly decreases, but the lattice structure remains unchanged, confirming a chemical reaction between MMT and CS. Under the influence of CS, the height and width of the peak at 2θ = 6.7° increase, indicating more crystal planes and stronger diffraction intensity. PA-Na shows no distinct XRD peaks, indicating its amorphous nature. Additionally, the characteristic peaks of MMT@CS@PA-Na remain unchanged, but its crystallinity is further reduced compared to MMT@CS. These results indicate that PA-Na chemically modifies MMT@CS, and the mild synthesis method minimally affects the MMT structure.

Analysis of the spectral profiles of a) XRD pattern, b) FT-IR pattern experimental materials.
Figure 4.
Analysis of the spectral profiles of a) XRD pattern, b) FT-IR pattern experimental materials.

The functional groups of the materials were analyzed by FTIR, as shown in Figure 4(b). The FTIR spectrum of CS exhibits a prominent and broad characteristic band in the vicinity of 3700-3000 cm1, which is associated with the stretching vibrations of O-H and N-H groups [30]. The characteristic bands located around 2925 cm1 and 1434 cm1 correspond to the symmetric and asymmetric stretching vibrations of C–H groups [31]. The bands at 1651 cm1 and 1024 cm1 are attributed to the stretching of C=O in amides and the asymmetric stretching of C-O-C, respectively [32,33]. Na-MMT shows a strong and broad characteristic band around 3750-3300 cm1, which is related to the stretching vibration of O-H groups. The sharp absorption peak at 3624 cm1 is due to the stretching vibration of the free hydroxyl group O-H, while the broad absorption peak at 3638 cm1 is attributed to the stretching vibration of intermolecular hydrogen-bonded O-H. The peak at 1646 cm1 is attributed to the stretching vibration of the C=C group, and the peak at 1032 cm1 is attributed to the stretching vibration of the Si-O-Si tetrahedral sheet group.

In the FTIR spectrum of Na-MMT@CS, a noticeable reduction in band intensity is observed in the range of 3650-3000 cm1, and the intensity of intermolecular hydrogen-bonded O-H at 3438 cm1 is diminished, confirming the successful grafting of CS onto the surface of Na-MMT. The Na-MMT@CS@PA-Na spectrum reveals characteristic peaks of PA-Na, with the energy bands shifting from 1105 cm1 (P=O) and 980 cm1 (C-O) to 1100 cm1 and 1020 cm1, respectively. It demonstrates the electrostatic interaction between PO3-4 in PA-Na and NH3+ in CS, indicating that PA-Na can successfully bind to CS and subsequently encapsulate the CS surface. The results validate the spontaneous microencapsulation of Na-MMT through ionic cross-linking between CS and PA-Na, synthesizing the microcapsule material Na-MMT@CS@PA-Na, successfully.

2.3.3. Pyrolysis reaction

The thermal effects of Na-MMT@CS@PA-Na at high temperatures, a HITACHI STA200 synchronous thermal analyzer was used to study the decomposition behavior of the microcapsule Na-MMT@CS@PA-Na powder using TG and DSC. Figure 5 shows that the TG-DTG-DSC curves of Na-MMT@CS@PA-Na.

TG-DTG-DSC spectra of experimental materials.
Figure 5.
TG-DTG-DSC spectra of experimental materials.

During the first stage, an endothermic peak appears within the temperature range of 23°C–112°C, with a peak temperature of 92°C and a corresponding specific heat capacity of 197 J/g. This stage is accompanied by an 11% mass loss, primarily attributed to the accelerated evaporation of adsorbed water on the powder surface and free water present within CS and PA-Na. The second stage, spanning 112°C to 437°C, involves a vigorous reaction with a 4% mass loss. During this phase, water molecules in the sample are substantially evaporated, and the -OH groups in PA-Na decompose, releasing H2O and initiating carbonization. Concurrently, the organic modifier chitosan begins to decompose, corresponding to the random cleavage of glycosidic bonds. Additionally, water molecules bound to Mg2+ cations in the octahedral coordination of montmorillonite are released. The third stage, from 437°C to 580°C, results in a 2% mass loss, during which the phytic acid groups decompose, the structure of montmorillonite is disrupted, and carbon participates in the reaction, leading to combustion and mass reduction. In the fourth stage, between 580°C and 670°C, the sample exhibits a mass loss rate of 3%. A minor endothermic peak is observed at 635°C, signifying the dehydroxylation of Na-MMT crystals and the reaction of carbon elements in PA-Na with molten NaPO3 to produce CO2 and gaseous phosphorus [34,35]. These reactions absorb combustion heat, resulting in the endothermic peak at 635°C. The fifth stage, occurring beyond 670°C, is characterized by negligible mass change, corresponding to the complete dehydration and dehydroxylation of Na-MMT crystals. The formation of refractory and stable products, such as MgSiO₃ and SiO₂, indicates the conclusion of the reaction process.

Throughout the decomposition process of Na-MMT@CS@PA-Na, the total mass loss amounts to 20%. This powder is capable of releasing combustion and radiant heat during the initial stages of coal dust explosion, and the residual products formed after decomposition can create a barrier that impedes heat and mass transfer.

3. Results and Discussion

3.1. Explosion flame propagation and pressure analysis of pulverized coal

Pre-experimental results indicate that when the coal dust concentration reaches 250g/m3, intense combustion on the flame surface rapidly spreads across the entire pipeline. The relationship of flame propagation and pressure increase during the coal dust explosion is illustrated in Figure 6. Following the discharge of the ignition electrode, the energy generated by the electric spark remains relatively low, resulting in a gradual vaporization rate of coal dust particles within the initial 4 milliseconds. Combustion intensifies at 31 milliseconds, with the flame contacting the sidewall of the pipeline and creating overexposed regions, accompanied by the onset of pressure increase. The maximum flame propagation velocity (Vmax) of 11.05 m/s is achieved at approximately 58 milliseconds, while the maximum rate of pressure rise ((dP/dt)max) reaches 11.5 kPa/ms. The peak flame front pressure (Pmax) of 50.5 kPa is attained at 67.5 milliseconds, which the yellow overexposed area progressively expands.

The relationship of flame propagation and pressure rise when c0 = 250g/m3.
Figure 6.
The relationship of flame propagation and pressure rise when c0 = 250g/m3.

However, with the decrease of oxygen concentration in the pipeline, the flame propagation rate gradually attenuates at this stage. Finally, the speed of the flame reaching the top of the pipeline (Vtop) is 3.3m/s at 85ms, and the average flame propagation rate (Vavg) of the whole process is 5.68 m/s.

3.2. Analysis of the influence on flame structure

Under the condition of coal dust concentration at 250 g/m3, Na-MMT@CS@PA-Na, as an explosion suppressant, demonstrates a significant impact on the flame propagation of coal dust explosions through its inserting ratio α (the ratio of the mass of Na-MMT@CS@PA-Na to the mass of coal dust). Figure 7 shows the sequence of coal dust explosion flame propagation after adding different inhibitors. At α=0.015, Na-MMT@CS@PA-Na significantly reduces the flame propagation height between 69ms and 190ms. In contrast, PA-Na alone shows flame propagation behavior nearly identical to that of pure coal dust, indicating its limited inhibitory efficacy. At α=0.030, PA-Na reduces the flame brightness, while Na-MMT induces flame irregularities and the formation of small-scale flame-free zones. The weak upward-propagating flame eventually ignites the remaining coal dust in the pipeline, forming clustered flames, indicating substantial hindrance to flame propagation in coal dust explosions. This observed phenomenon clearly demonstrates that Na-MMT@CS@PA-Na substantially impedes flame propagation by destabilizing combustion dynamics and interrupting spatial flame continuity.

Flame images of coal dust mixed with different inhibitor powders.
Figure 7.
Flame images of coal dust mixed with different inhibitor powders.

The passivation rate reached 0.045, during the period of 31∼67ms, the addition of PA-Na caused the flame front to become discrete. At 104ms, a significantly bright combustion zone appeared, which completely disappeared upon the incorporation of Na-MMT@CS@PA-Na. In the phase of 20∼190ms, a dark red flame emerged and floated to the middle section of the tube between 126∼273ms. Additionally, attributed to the dual mechanisms of oxygen deprivation and physical barrier formation introduced by Na-MMT@CS@PA-Na, the flame propagation within the pipeline exhibits discontinuity, with 0.045 being the optimal inserting ratio value.

3.3. Analysis of the influence on flame propagation behavior

Figure 8 illustrates the flame propagation velocity of lignite dust mixed with various inhibitors at different inserting rates α. The diagram demonstrates that as the inserting rate of each inhibitor increases, the diffusion time of the flame front is prolonged. The gasification and combustion of coal dust particles create unstable gas solid two-phase flames, causing varying degrees of pulsation in flame propagation. When the α value of Na-MMT reaches 0.045, the flame propagation velocity of Na-MMT is lower than the average velocity of 1.469 m/s, and the velocity exhibits significant oscillations. However, during the attenuation phase, the limited effect of Na-MMT causes a sharp rebound in flame velocity. For Na-MMT@CS@PA-Na, the flame propagation velocity exhibited negative values, with a decline observed in the position of the explosion flame front during the middle and late stages. It indicates that Na-MMT@CS@PA-Na significantly reduces the reaction rate of coal dust, demonstrating superior suppression efficacy compared to both Na-MMT and PA-Na.

(a-f) Flame propagation speed and height of coal dust mixed with different inhibitor powders.
Figure 8.
(a-f) Flame propagation speed and height of coal dust mixed with different inhibitor powders.

Figure 9 demonstrates that the inhibitor significantly reduces the propagation velocity of coal dust explosion flames (Vmax, Vtop, Vavg). When α=0.015, Na-MMT shows superior inhibition performance than PA-Na, with Na-MMT@CS@PA-Na reducing Vmax, Vtop, and Vavg by 45.26%, 11.43%, and 60.97% respectively, indicating that minimal addition of a single inhibitor has limited effectiveness. As α increases to 0.045, PA-Na, Na-MMT, and Na-MMT@CS@PA-Na reduce Vmax by 24.59%, 68.92%, and 70.93%, respectively, Vtop by 87.95%, 35.5%, and 57.14%, and Vavg by 46.74%, 74.09%, and 89.59%. In summary, Na-MMT@CS@PA-Na significantly outperforms PA-Na and Na-MMT in mitigating flame propagation velocity, demonstrating optimal inhibitory performance.

(a-c) The inhibitory effect of explosion suppressants on the characteristic value of flame propagation speed in coal dust explosions.
Figure 9.
(a-c) The inhibitory effect of explosion suppressants on the characteristic value of flame propagation speed in coal dust explosions.

3.4. Analysis of the influence on flame temperature

Flame temperature serves as a critical indicator of combustion reaction intensity. Figure 10 illustrates the flame temperature variations during the explosion of coal dust and inhibitor mixtures. For PA-Na powder, as the α value increased from 0.015 to 0.045, the peak temperature decreased from 584°C to 473°C, representing a reduction of 111°C, yet remained above 300°C. In contrast, Na-MMT with an α of 0.045 reduced the peak temperature below 300°C. Na-MMT@CS@PA-Na exhibited the most effective suppression of flame temperature. At α=0.030, the peak temperature decreased to 278°C, and at α=0.045, it further dropped to 89°C. This dramatic temperature reduction substantially hindered contact between coal dust particles, weakened the heat transfer process, and consequently suppressed the gaseous combustion reaction and flame temperature.

(a-c) The flame temperature variation of coal dust/inhibitor mixture explosion.
Figure 10.
(a-c) The flame temperature variation of coal dust/inhibitor mixture explosion.

3.5. Influence analysis of explosion suppression materials on flame pressure change

The experiment maintained a powder concentration of 250 g/m3 and atmospheric pressure prior to the explosion. Upon detonation, the rapidly expanding airflow within the confined conduit accelerated the flame, with energy enhancement achieved through the compression of the airflow ahead of the flame, resulting in the formation of pre-flame pressure. Figure 11 clearly illustrates the temporal variation of pre-flame pressure after the explosion of the inhibitor or coal dust mixture. Analysis of the suppression curves reveals that the incorporation of either Na-MMT or PA-Na alone yields limited efficacy in mitigating coal dust explosions. However, with the addition of suppressants, the maximum explosion pressure of coal dust was significantly reduced, the rate of pressure rise markedly decelerated, the time to reach peak explosion pressure was prolonged, and the overall explosion reaction was effectively suppressed.

(a-c) The pressure changes of coal dust/inhibitor mixture explosion.
Figure 11.
(a-c) The pressure changes of coal dust/inhibitor mixture explosion.

The reduction in explosion pressure follows an increasing order from PA-Na, Na-MMT, to Na-MMT@CS@PA-Na, with Na-MMT@CS@PA-Na demonstrating the most superior explosion suppression performance. This is attributed to its modified particle structure: montmorillonite exhibits excellent heat absorption properties and undergoes endothermic decomposition during the explosion process. The decomposition releases inert gases which retard radical recombination, thus suppressing the explosion reaction.

The comparative analysis of explosion pressure suppression efficacy is illustrated in Figure 12. The graphical representation demonstrates a negative correlation between Pmax, (dP/dt)max, and the increasing inserting rate of inhibitors. Upon the addition of PA-Na and Na-MMT with an inserting rate of 0.045, the Pmax of coal dust particles was reduced by 22.1% and 74%, respectively. When the inserting rates of Na-MMT@CS@PA-Na were 0.015, 0.030, and 0.045, Pmax decreased by 46.5%, 61.3%, and 92.9%, while (dP/dt)max decreased by 57.2%, 67.7%, and 94.64%, respectively. The unique coupling mechanism of Na-MMT@CS@PA-Na produces synergistic suppression effects: its endothermic properties lower the ambient temperature, oxygen dilution reduces combustible gas concentrations, and thermal insulation impedes heat transfer. Collectively, these effects constrain the coal dust explosion reaction. This leads to reduced flame propagation velocity and heat release, substantial attenuation of energy accumulation at the flame front, and ultimately, effective inhibition of explosion intensity.

Maximum explosion pressure and maximum pressure rise rate of coal dust/inhibitor mixtures under different inserting ratios.
Figure 12.
Maximum explosion pressure and maximum pressure rise rate of coal dust/inhibitor mixtures under different inserting ratios.

3.6. Analysis of explosive products

Figure 13 shows the microscopic morphology comparison of the explosion products of coal dust before and after the addition of inhibitors. After the explosion, the surface of pure coal dust powder becomes rough and has distinct edges. There are a large number of particles in the explosion residue, and some of the particles are dispersed on the surface of uncompletely burned coal dust particles. The fine pores observed on the surface of the coal dust particles are attributed to the release of volatile matter from within the particles during heating, which escaped through the particle surface.

SEM image of explosive residue: Coal; Coal +Na MMT; Coal +PA-Na; Coal + Na-MMT@CS@PA-Na.
Figure 13.
SEM image of explosive residue: Coal; Coal +Na MMT; Coal +PA-Na; Coal + Na-MMT@CS@PA-Na.

After adding Na-MMT, the surface of the coal dust was encapsulated by Na-MMT, which was smooth without any pits, and there was a significant adhesion phenomenon between the particles. Compared to pure coal dust, the edges were less obvious. The explosive residue after adding PA-Na was composed of a dense flocculent structure. This indirectly revealed that the high temperature generated during the coal dust explosion led to the rapid thermal decomposition of PA-Na to produce gaseous products, carbon layers and phosphates. As shown in the figure, Na-MMT@CS@PA-Na still maintained a relatively good blocky structure in the explosive residue, with uniformly adhered agglomerated particles on the surface. Moreover, Na-MMT@CS@PA-Na was laid horizontally on the coal dust particles, and the tiny size of the coal dust was significantly larger than that of the explosive residues of pure coal dust in previous studies. This directly verified that Na-MMT@CS@PA-Na effectively weakened the gas-phase combustion reaction of coal dust.

4. Conclusions

This study examines the inhibitory effect of microencapsulated suppressant Na-MMT@CS@PA-Na on lignite dust explosions through characterization and experiments. Using a dust explosion test system, it investigates the material’s influence on flame propagation, temperature variation, and pressure characteristics, providing theoretical and technical support for developing novel coal dust suppressants.

The experimental synthesis method was employed to adsorb CS and PA-Na target particles onto the surface layer of Na-MMT. Characterization studies using SEM, XRD, FTIR, and TG demonstrated significant changes in the surface morphology and chemical groups of Na-MMT, confirming the successful preparation of the microencapsulated explosion suppressant.

The flame propagation height of Na-MMT@CS@PA-Na was significantly suppressed at inserting rates of 0.015 and 0.030. When the inserting rate increased to 0.045, the luminous combustion zone completely disappeared, and the flameless region at the bottom of the pipeline expanded.

With the increase in inhibitor passivation rate, the diffusion time of the flame front is prolonged, the propagation velocity is reduced, and a pulsation effect is observed. When the passivation rate α=0.045, the inhibitory effects of PA-Na, Na-MMT, and Na-MMT@CS@PA-Na on the flame propagation velocity parameters exhibit variations. In terms of suppressing flame temperature and coal dust explosion pressure, the composite inhibitor Na-MMT@CS@PA-Na demonstrates significantly superior performance compared to single-component materials.

Acknowledgment

The research presented in this paper was supported by National Natural Science Foundation of China (No.52274205,52474225), LiaoNing Revitalization Talents Program (No.XLYC2203176).

CRediT authorship contribution statement

Yujiao Liu: Investigation, Resources and Supervision. Mingyi Li: Writing-Original draft preparation,Data Curation, and Validation. Ke Gao: Resources, Writing-Review and Editing, Supervision, Project administration, and Funding acquisition. Lu Chen: Data Curation, Validation and Supervision.

Declaration of competing interest

The authors declare no conflicts of interest.

Declaration of generative AI and AI-assisted technologies in the writing process

The authors confirm that there was no use of artificial intelligence (AI)-assisted technology for assisting in the writing or editing of the manuscript and no images were manipulated using AI.

References

  1. , , , , , , , , . Effect of vent burst pressure on the external overpressure behaviors and flame transients of vented petroleum fuel-air mixture explosion: Small-scale study. Energy. 2025;335:138095. https://doi.org/10.1016/j.energy.2025.138095
    [Google Scholar]
  2. , , , , , . Experimental study on effect of dilute coal dust on gas explosion pressure/flame evolution process. Powder Technology. 2022;404:117450. https://doi.org/10.1016/j.powtec.2022.117450
    [Google Scholar]
  3. , , . Study on the influence of coal dust particle size on the structure and propagation characteristics of explosion flame in Hartmann tube. Arabian Journal of Chemistry. 2025;18:902024. https://doi.org/10.25259/ajc_90_2024
    [Google Scholar]
  4. , , , , , . The effects of different equivalence ratios and initial pressures on the explosion of methane/air premixed gas in closed space. Energy. 2024;297:131213. https://doi.org/10.1016/j.energy.2024.131213
    [Google Scholar]
  5. , , . Prevention and control effects of ultra-fine CaCO3 inserting agent on dust explosion during aluminum alloy polishing [J] China Safety Production Science Technology. 2022;18:140-146. https://doi.org/1010.11731/j.issn.1673-193x.2022.09.020
    [Google Scholar]
  6. , , , , , , . Experimental and theoretical studies on the effect of Al(OH)3 on the fire-extinguishing performance of superfine ABC dry powder. Powder Technology. 2021;393:280-290. https://doi.org/10.1016/j.powtec.2021.05.075
    [Google Scholar]
  7. , , , , , , , . Experimental study on the ression of coal dust explosion by silica aerogel. Energy. 2023;267:126372. https://doi.org/10.1016/j.energy.2022.126372
    [Google Scholar]
  8. , , . Research on the explosion suppression and gas ablation of catalytic adsorption composite powders CuO-CeO2/CaO. Coal Science and Technology. 2025;53:122-134. https://doi.org/10.12438/cst.2025-0249
    [Google Scholar]
  9. , , , . Chemical vapor deposition-based synthesis of binder-free nanostructure -MoO3 electrode material for PES devices. Physica Scripta. 2024;99 https://doi.org/10.1088/1402-4896/ad3502
    [Google Scholar]
  10. , , . Enriched pseudocapacitive performance of CVD deposited MoSe2/MoS2 heterostructured binder free nanospheres for asymmetric supercapacitor applications. Journal of Physics and Chemistry of Solids. 2026;208:113138. https://doi.org/10.1016/j.jpcs.2025.113138
    [Google Scholar]
  11. , , , , . Effect of cerium doping on optical and electrochemical properties of nickel oxide nanostructures. Ionics. 2025;31:7479-7492. https://doi.org/10.1007/s11581-025-06365-3
    [Google Scholar]
  12. , , , . Hydrothermal tellurization process for crafting nanostructured cobalt telluride: A hop advancing in supercapacitor and non-enzymatic glucose sensor. Materials Research Bulletin. 2025;187:113359. https://doi.org/10.1016/j.materresbull.2025.113359
    [Google Scholar]
  13. . Experimental study on the use of diatomaceous earth-based composite powder as an explosion inhibitor for gas explosions. Coal Technology. 2025;44 https://doi.org/10.13301/j.cnki.ct.2025.02.022.
    [Google Scholar]
  14. , , , , , , , . Study on the inhibition of explosion and combustion of coal dust based on the structure of core-shell microencapsulated polyurethane. Energy. 2024;290:130159. https://doi.org/10.1016/j.energy.2023.130159
    [Google Scholar]
  15. , , . Synthesis and application research progress of microcapsules. Petrochemical Application. 2025;44:10-13+36. https://doi.org/10.1016/j.issn.1673-5285.2025.03.002
    [Google Scholar]
  16. , , , , , , . Research progress on ammonium polyphosphate and its synergistic agents for flame retardant polylactic acid. Journal of Composite Materials. 2025;42:4855-4868. https://doi.org/10.1016//j.cnki.fhclxb.20250116.002.
    [Google Scholar]
  17. , , , et al. Surface activity agent-modified montmorillonite adsorption of phenol performance and structural characterization. Acta Mineralogica Sinica 2025:1-14. https://doi.org/10.3724/j.1000-4734.2025.45.011
    [Google Scholar]
  18. , , . Suppression of methane explosion in pipeline network by carbon dioxide-driven calcified mont⁃morillonite powder. Arabian Journal of Chemistry. 2022;15:104126. https://doi.org/10.1016/j.arabjc.2022.104126
    [Google Scholar]
  19. , , . Molecular dynamics simulation on CO2 hydrate growth and CH4-CO2 replacement in various clay nanopores. Energy. 2025;314:134282. https://doi.org/10.1016/j.energy.2024.134282
    [Google Scholar]
  20. , , . Suppression of methane explosion in pipeline network by carbon dioxide-driven calcified montmorillonite powder. Arabian Journal of Chemistry. 2022;15:104126. https://doi.org/10.1016/j.arabjc.2022.104126
    [Google Scholar]
  21. , , , , , , . The preferential adsorption mechanisms of montmorillonite and hematite on the dissolved organic matter derived from aged biochar. Acta Agronomica Sinica. 2025;44:1563-1570. https://doi.org/10.1016/jaes.2024-0653.
    [Google Scholar]
  22. , , , , , , . Study on the effects of montmorillonite, reservoir clay and calcite on crude oil cracking. Geochemistry. 2025;54:785-800. https://doi.org/10.19700/j.0379-1726.2024.01.160.
    [Google Scholar]
  23. , , , , , , . Synergistic MMT-MnO2 coating design for dual enhancement of polysulfide conversion and lithium-ion diffusion in Li-S batteries. Sustainable Materials and Technologies. 2025;46:e01736. https://doi.org/10.1016/j.susmat.2025.e01736
    [Google Scholar]
  24. , , , , , , , . Study on Al powder explosion suppression mechanism of MCA@ADP-MMT composite. Journal of Loss Prevention in the Process Industries. 2026;100:105873. https://doi.org/10.1016/j.jlp.2025.105873
    [Google Scholar]
  25. , , , , , , , , , , . Multi-functional flame retardant coatings comprising chitosan/gelatin and sodium phytate for rigid polyurethane foams. Journal of Cleaner Production. 2023;394:136371. https://doi.org/10.1016/j.jclepro.2023.136371
    [Google Scholar]
  26. , . The effect of the number of assembly layers of chitosan/sodium phytate/nanoMgO composite coatings on the flame retardant properties of wood. Furniture. 2021;42:48-51. https://doi.org/10.16610/j.cnki.jiaju.2021.02.011.
    [Google Scholar]
  27. , , , , . Preparation of carbon-based cathode materials for new energy batteries by thermally decomposing sodium phytate. Journal of Chengdu University. 2019;38:409-413. https://doi.org/10.3969/jissn.10045422.2019.04.016.
    [Google Scholar]
  28. , , , , , , , , . Study on the inhibition mechanism of green suppressants zinc borate and zinc silicate for oil shale based on flame propagation experiment and thermodynamic analysis. Energy. 2023;283:129014. https://doi.org/10.1016/j.energy.2023.129014
    [Google Scholar]
  29. , , . High antibacterial activity of chitosan-molybdenum disulfide nanocomposite. Carbohydrate Polymers. 2019;215:226-234. https://doi.org/10.1016/j.carbpol.2019.03.085
    [Google Scholar]
  30. , , , , , , , , . Fabrication and application of chitosan-based biomass composites with fire safety, water treatment and antibacterial properties. International Journal of Biological Macromolecules. 2023;225:266-276. https://doi.org/10.1016/j.ijbiomac.2022.10.261
    [Google Scholar]
  31. , . Chitosan pyrolysis and adsorption properties of chitosan and its carbonizate. Carbohydrate Research. 2010;345:941-947. https://doi.org/10.1016/j.carres.2010.02.024
    [Google Scholar]
  32. , , , , , , , , , , , . Ultra-fine carbon decorated TiO2/C/g-C3N4 hybrid for strong physical adsorption and efficient photodegradation of pollutants. Arabian Journal of Chemistry. 2025;18:106034. https://doi.org/10.1016/j.arabjc.2024.106034
    [Google Scholar]
  33. , , , , , , . Interactions between alginate and chitosan biopolymers characterized using FTIR and XPS. Biomacromolecules. 2007;8:2533-2541. https://doi.org/10.1021/bm070014y
    [Google Scholar]
  34. , , , , . Characterization of microscopic adsorption of CH4/O2 on lignite based on molecular dynamics. Arabian Journal of Chemistry. 2025;18:483. https://doi.org/10.25259
    [Google Scholar]
  35. . Study on the effect of functional group modification on the methane inhibiting and detonation suppression properties of montmorillonite powder. Henan Polytechnic University. 2020 https://doi.org/10.27116/d.cnki.gjzgc.2020.000143
    [Google Scholar]
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