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On the Effectiveness of Aerosol Extinguishing Agents for Battery Vent Gases and Hydrogen

  • Open Access
  • 16.01.2025
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Abstract

Der Artikel untersucht die Effizienz von Kaliumkarbonat-Aerosolen bei der Unterdrückung von Bränden mit Gasen aus Wasserstoff und Lithium-Ionen-Batterien. Es kombiniert experimentelle und Simulationsmethoden, um die chemischen und physikalischen Mechanismen der Flammenunterdrückung zu analysieren. Die Studie konzentriert sich auf die Zersetzungs- und Radikalspaltungsprozesse von Kaliumcarbonaten und hebt deren überlegene Löschfähigkeit im Vergleich zu Halonen hervor. Die Forschung befasst sich auch mit den Herausforderungen durch den hohen Wasserstoffgehalt in Batterieentlüftungsgasen, der zu erhöhten Verbrennungsgeschwindigkeiten und Instabilitäten führen kann. Der Artikel bietet ein umfassendes Verständnis der Unterdrückungsmechanismen und der Bedingungen, unter denen Aerosole am effektivsten sind, und trägt zur Entwicklung sichererer Brandbekämpfungsstrategien für neue Energieträger bei.

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1 Introduction

The use of new energy carriers, such as hydrogen and lithium-ion batteries (LIB), presents new safety challenges that require updated guidance for the prevention of fire incidents. An important step in addressing these challenges is to investigate the efficiency of established suppression methods when applied to fire events involving these new energy carriers. Although widely used in fire suppression systems, potassium-based aerosols have not been extensively studied by the scientific community. Studies indicate that alkali metal carbonates, such as sodium and potassium carbonates, are effective substitutes for halons in suppression systems [1, 2]. Experimental results indicate that sodium carbonate has a superior mass-based extinguishing efficiency compared to halon 1301 [1]. Likewise, potassium carbonate aerosols are highly effective at suppressing diffusion flames, with an efficiency per unit weight of 3–10 times greater than that of halon 1301 [2]. Because of their proven effectiveness, potassium compounds are the primary constituents of several commercial fire suppression compositions, either with potassium bicarbonate, KHCO3, or dipotassium carbonate, K2CO3. The aerosols, when heated to approx. 900⁰C decomposes into gas phase products, and the fire suppression is achieved as a result of a radical scavenging process consuming OH radicals but potentially also H and O [3]. The sequence of events leading to flame extinguishment with aerosols begins with the distribution of the aerosol within the enclosure, followed by heating and subsequent decomposition of the aerosols, and finally, interactions with radical chemistry.
According to the literature [4], the decomposition of K2CO3 takes place with reaction 1, where the product in a moist environment forms KOH through reaction 2. Both K2O and KOH can then react with a range of radicals and stable components in the flame, to form K-radical which has a flame-retardant effect through efficient consumption of OH radical in the chain termination reaction 3.
$${\text{K}}_{{2}} {\text{CO}}_{{3}} \to {\text{K}}_{{2}} {\text{O}} + {\text{CO}}_{{2}}$$
(1)
$${\text{K}}_{{2}} {\text{O }} + {\text{ H}}_{{2}} {\text{O}} \to {\text{2 KOH}}$$
(2)
$${\text{OH}} + {\text{K}} + {\text{M}} \to {\text{KOH}} + {\text{M}}$$
(3)
Following these reactions, the KOH will further react with radicals OH and H, decreasing the overall pool of reactive radicals sustaining the fire. The inhibition effects are both physical and chemical. The physical effect is primarily achieved through heat absorption [5]. The chemical effect of potassium carbonates is highly efficient in flame inhibition in the gas phase, as the process is auto-catalytic. Mechanistic studies on the homogeneous gas phase process include the chemical kinetics mechanism [3], its effect on strain rate [6], and time-scale analysis [7]. An important step before homogeneous flame inhibition is the thermal decomposition of the particles, as investigated for the analogous Na2CO3 by Dounia et al. [8]. The effect of aerosol particle size on KHCO3 has been studied by Zhou et al. [9], and it was concluded that a decrease in particle size improved fire suppression. The smaller particles decomposed at lower temperatures and absorbed more heat than the larger particles, resulting in larger amounts of reactive radicals available for chemical fire suppression. It is also noteworthy that an experimental study on bicarbonates indicates that potassium carbonates are superior to sodium carbonates [10]. A review by Zhang et al. [11] focuses on various fire extinguishing agents that they categorize as “hot aerosols,” which include potassium-based aerosols. In a review by Rohilla et al. [12] covering common agents from a general fire perspective, potassium is both mentioned as an ingredient in advanced “Aerosol Forming Composition” and as an extinguishing agent on its own belonging to a group named “chemical powders”.
The fire risk related to Li-ion batteries is associated with when the batteries enter a state known as thermal runaway, which involves uncontrolled heat and gas production that can lead to fire or, in instances of delayed ignition, gas explosions. Li-ion batteries contain a range of chemical substances, a large proportion of which are flammable, such as dimethyl carbonate (CH3OC(O)OCH3), and smaller amounts are toxic substances such as lithium phosphorus hexafluoride (LiPF6). During the thermal runaway, uncontrolled chemical reactions occur between different chemical substances in the battery, which results in the formation of new flammable and toxic reaction products as well as a large amount of heat. The breakdown of large stable molecules into smaller and more volatile ones leads to an increase in pressure inside the battery cell, which is further exacerbated by the increased temperature. In thermal runaway, not only are the flammable gases hydrogen (H2) and carbon monoxide (CO) and the inert carbon dioxide (CO2) primarily produced, but a significant proportion of methane (CH4), ethylene (C2H4), and other gaseous hydrocarbons is also formed [13]. Among the toxic components, hydrogen fluoride (HF) can be mentioned in particular.
The proportion of different types of gases formed in a lithium-ion battery during thermal runaway depends on several factors, such as the type of cell chemistry and the state of charge (SOC). LIB with a lower SOC emits smaller volumes of gas with a less flammable composition as compared to highly charged batteries [14]. The variation in the composition of the vented gases suggests that the effectiveness of extinguishing agents may also vary, and their effectiveness likely depends on whether the agent is applied to a fire (diffusion flame) or to prevent gas explosions (premixed flame). Generally, there is also a notable variation in the extinguishing efficiency of different agents when applied at the cell level compared to the module and rack levels [15]. Comprehensive review studies on fire-extinguishing agents for suppressing lithium-ion battery fires have been conducted by Majeed et al. [16] and Yuan et al. [17], highlighting the essential design principles for effective fire-extinguishing agents and evaluating various options. However, these reviews do not address potassium carbonates. The present work investigates the effects of applying dipotassium carbonate K2CO3 to a premixed flame, simulating a gas explosion due to delayed ignition. This compound is more efficient than potassium bicarbonate, KHCO3 [3]. The experiments are performed with aerosols with a diameter of around 1 µm since a recent literature review suggests that aerosols with a size in the order of 10 µm are generally ineffective for pure hydrogen flames, as they do not evaporate before reaching the flame unless hydrocarbons are added [18].
Combustion characteristics of gases vented from Li-ion batteries were recently investigated in a simulation study by Nilsson et al. [13]. As part of that study, the compositions of battery vent gases were reviewed, and typical cases were selected for ignition and flame simulations. Batteries with LFP (Lithium iron phosphate) and NCA (Lithium nickel cobalt aluminum oxide) chemistries, studied experimentally by Lammers et al. [19] were found to produce the least and most flammable vent gas mixtures, respectively, which was demonstrated by the determination of laminar burning velocities by Henriksen et al. [20]. The variation in flammability of the vent gases depends on the balance between the inert CO2 on one hand, and the highly flammable CO and H2 on the other hand. At 100% SOC, the gases from an LFP battery were found to consist of approximately 48% CO2, 9% CO, and 30% H2, while a high-energy NCA battery has less CO2 and more flammable gases, namely 10% CO2, 37% CO and 43% H2. The highly reactive gas mixture from NCA has a burning velocity that is about three times higher than that of the gas mixture from the LFP battery. The high hydrogen content also leads to the flame having a high burning velocity even at low oxygen concentrations (at a high equivalence ratio number). The combustion is driven by radicals that arise in the flame front, mainly O, H, and OH. The hydroxyl radical, OH, is counted in most combustion cases as the most important radical for maintaining flame propagation. However, the study clearly shows that for the highly reactive mixture with a high hydrogen content, the H radical also has great importance when there is a lack of oxygen.
Considering the high amount of H2 in the most flammable gas mixtures from lithium-ion batteries, and the fact that H2 itself is an important energy carrier becoming increasingly used, the efficiency of flame extinguishing media on high-H2 gas mixtures needs to be studied. In the present work, an experimental study on the effect of K2CO3 aerosols on the flames for the mixtures between air and a gas mixture mimicking vented gases from an NCA battery1 as well as pure H2 is presented. To increase the understanding of the effect of the aerosol-generating fire extinguisher on premixed flames, the experiments were designed to simulate a gas explosion using a well-controlled laminar setup as suggested by [18]. Experiments with methane (CH4) are also performed as a reference as well as CO2 as an alternative suppressant. To further understand the chemical effects in the flame-extinguishing process, chemical kinetics simulations were performed for both the NCA-, LFP-, and pure H2-mixture to elucidate the pure chemical gas phase effects under the assumption that the aerosol is completely evaporated.

2 Materials and Methods

2.1 Experimental Setup

As shown in Fig. 1, a three-line configuration was used to inject the flammable oxidizers (O2 gas), and inert gases (N2 gas) separately into a mixing tube. The cylindrical premixing tube, with an inner diameter of 5 mm and 200 mm in length, is equipped with an aerosol injector 50 mm downstream of the junction of three lines. The flammable gas and oxidizer are injected in a counterflow manner while the inert gas is injected vertically upwards upstream of the mixing tube. A cuboid-shaped tube with a square cross-section of 10  cm2× 10 cm2 and a length of 50 cm is placed on the metal base plate at the premixing tube's outlet. The cuboid-shaped tube is made of quartz to provide optical access for optical measurements and mitigate the effect of surrounding air on the flame at the mixing tube outlet.
Figure 1
Schematic for flow configuration and experimental setup
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The suppression aerosol utilized here was a commercially available product based on potassium carbonate (K2CO3). Upon release, the particles have a mean diameter of 0.8 µm, but within the first 10 min, they agglomerate to particles with a mean diameter of 1.5 µm. The experiments were performed after this initial agglomeration process to ensure consistent experiments and to be representative of a delayed ignition scenario. To allow controlled injection of aerosols, the aerosols were first dispersed in a separate steel cylinder with a diameter of 400 mm and length of 1.5 m. The cylinder was divided into two compartments separated by a Teflon membrane. Before the activation of the aerosol into the cylinder, the air-side of the membrane was filled with 0.08 m3 of air. As the aerosol was released into the aerosol-side of the cylinder, the air in the air-side of the membrane was opened to the surrounding, and then a vacuum pump was used to remove the remaining air. While the air was extracted, a connection between the ambient and the aerosol-side was opened to replace the air being removed (but on the other side of the membrane). Since the effective amount of aerosol and the volume were known, the concentration could be calculated and since the final volume of the aerosol-side of the membrane was 0.126 m3 and the effective mass of the aerosol injector was 24.8 g, the concentration in the cylinder was calculated as 132 g/m3. The actual concentration might also be smaller due to deposition so mainly trends and not actual suppression concentrations can be investigated.
A sketch of the optical setup employed in the experiments is shown in Fig. 1. The flame structure was visualized using PLIF imaging of OH radicals, indicating the reaction and post-flame zones. OH-PLIF measurements were performed by exciting the Q1(8) transition of the OH radicals employing 283 nm laser radiation. A frequency-doubled (532 nm) Nd: YAG laser was used to pump a tenable dye laser (operated with Rhodamine 590 dye). The output of the dye laser (566 nm) was frequency-doubled and tuned to the Q1 (8) transition. The approximately 100 mm wide laser sheet was formed using sheet forming optics (a − 40 mm cylindrical and a + 500 mm spherical lens) and guided through the mid-plane of the burner exit. The laser pulse energy varied between 14 and 16 mJ during the measurements. The OH-PLIF signals were detected using an ICMOS camera (Andor iStar SCMOS) with a native resolution of 2560 × 2160 pixels with an individual pixel size of 20 μm and 16-bit. The resolution was reduced using on-chip binning to 1280 × 1080 pixels allowing for a higher signal-to-noise ratio (SNR). The PLIF images were collected at a frequency of 20 Hz. A UV-Nikkor lens was used with a focal length of 105 mm and a f-number set to 4.5. A 320 ± 20 nm bandpass filter was fixed to eliminate interference signals. For each flame condition, 200 single-shot PLIF images were collected at a frequency of 20 Hz. The scaling factor of the acquired images was 0.13 mm/pixel.

2.2 Experimental Methodology

To understand the effect of dipotassium carbonate (K2CO3) aerosols on premixed flames, experiments were designed to simulate a gas explosion due to delayed ignition. The target gases were those emitted from thermal runaway in LIB based on NCA chemistry as well as H2. Reference measurements were accomplished by employing CH4 flame and CO2 as flame quenchers. Investigations on flammable gases CH4 (as a reference case), pure H2, and the gas mixture, mimicking vented gases, were performed at the most stable flame conditions at room temperature by varying flow velocity (Vf) at the mixing tube exit, and the equivalence ratio (ϕ), which is the normalized actual fuel–air ratio by the stoichiometric fuel–air ratio. As synthetic air, pure N2, and O2 were injected according to the air composition ratio of 1:3.76 and mixed with the flammable gas mixture in the premixing tube before initiating ignition. The equivalence ratio (ϕ) was varied by changing the ratio of flammable gas and synthetic air in the premixed mixture. The flow velocity at the mixing tube exit was calculated by dividing the required volume flow by the premixing tube’s exit area. The composition of the gas mixture, mimicking vented gases, as well as ranges of variation for Vf, and ϕ are tabulated in Table 1. At different flow velocities, the equivalence ratio was varied to identify the critical ratios where flame behaviors are most stable. To investigate the equivalence ratio that produces the most stable flame, the equivalence ratio was increased by adjusting the air and fuel flow rates while maintaining a constant Reynolds number.
Table 1
Compositions of Flammable Gas Mixtures, Ranges of Variation for Vf, and ϕ
Flammable gas/mixtures
CO2 (Vol%)
CO (Vol%)
H2 (Vol%)
CH4 (Vol%)
C2H4 (Vol%)
C2H6 (Vol%)
Temperature (T) (°C)
Exit Velocity (Vf) (m/s)
Reynolds number (Re) (–)
Equivalence ratio (ϕ)
Aerosol concentration (g/cm3)
CH4
0
0
0
100
0
0
25
2.5
362
1
0–79.2
Synthetic battery vent gas
10
37.1
42.8
7.1
3
0
25
5
725
0.7
0–79.2
H2
0
0
100
0
0
0
25
5 & 10
725 & 1450
0.4–0.5
0–79.2
For each flame condition, two sets of measurements were performed: one soon after releasing the aerosol and another two hours post-activation, to understand how deposition, and therefore indirectly the size distribution of the aerosol, affected the flame.
To measure the effect of the aerosol on the combustion of the mixture, the burning velocity was calculated using the Bunsen burner approach which has been widely used in previous studies [2123]. The laminar burning velocity is defined as the velocity at which a planar flame front travels toward the unburned gas in a direction normal to the flame surface [24]. When the flame is stationary, it is stabilized by forming a conical shape at the end of the duct of a Bunsen burner. In Fig. 2, the cross-section of the Bunsen burner shows the streamlines indicating the propagation of the reactant mixture which consists of gaseous fuel and air.
Figure 2
Bunsen burner cross-section
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Now, if \({V}_{f}\) denotes the velocity of the reactant mixture and \(2\alpha\) is the angle of the cone formed by the flame surface, the laminar burning velocity \({S}_{L}\) can be determined by the velocity component of the reactant mixture orthogonal to the flame surface [2527].
$$S_{L} = V_{f} \cdot sin\left( \alpha \right)$$
(4)
In this study, the angle of the cone formed by the flame surface was calculated from the OH-PLIF images of Bunsen flames. The OH radicals are one of the most important intermediate reactants during combustion. The distribution of OH can be used to determine the reaction zone [28]. Images of OH also represent the boundary of hot products with cold reactants, and the flame front can be extracted from OH images by processing the signal gradient [29]. An example of an acquired OH-PLIF image is presented in Fig. 3b. The flame exhibits axial symmetry around the burner center, and the OH-PLIF image was bisected along this center (refer to Fig. 3c). To determine the burning velocity, an edge detection program in MATLAB was utilized to identify the reaction zone by detecting the maximum derivative of the OH-PLIF signal intensity along the flame's radius (see Fig. 3d). A polynomial line was then fitted to the points within the reaction zone (refer to Fig. 3d). Following this, a straight line was drawn on each side of the reaction zone using a simple linear regression model (see Fig. 3e). Finally, the inner cone formed between these two lines was calculated to measure the burning velocity according to Eq. 4.
Figure 3
Flame reaction zone determination: (a) Bunsen flame (b) OH-PLIF image of Bunsen flame, (c) the half of the OH-PLIF image, (d) points in the reaction zone decided by the edge detection program, (e) polynomial fit to the reaction zone, (f) linear regression modeling to draw a straight line
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2.3 Modeling

The chemical mechanism for the combustion of battery gases was adopted from the literature, and for more information on this, including validation of the reliability of the mechanism, refer to [13]. To investigate the effect of K2CO3 on flame behavior, the battery gas reaction mechanism was combined with a subset of K-chemistry developed by Babushok et al. [3]. The gas mixtures studied were the same as for the experiments: high reactive (NCA) battery gas (as defined in Table 1) pure hydrogen and pure methane. One additional gas mixture representative of a less reactive (LFP) battery gas, consisting of 48% CO2, 9% CO, and 30% H2, was also included. As mentioned in the introduction, this was also intended for the experimental study but could not be performed due to heat loss to the pipe preventing steady burning.
The simulations were carried out with initial concentrations of K2CO3 corresponding to an aerosol quantity of a maximum of 130 g/m3 and a minimum of one-hundredth of this concentration. This corresponds to a range from 10 mass-% down to 0.1 mass-% aerosol in air. In the simulations, it is assumed that the aerosol is gasified when it reaches the flame/ignition point.
The Chemkin Pro software was used for all simulations and the premixed flames were simulated with the PREMIX code. All simulations were performed using a mixture-average (MIX) description of transport. Grid independence of the simulations was ensured by increasing the number of grid points until differences in results were less than 1%.

3 Results

3.1 Experimental Results

In the first tests, methane (CH4) was used as a reference flame to investigate the effect of aerosols. Figure 4 shows OH-PLIF images for CH4 flame when the synthetic air (N2 + O2) was replaced by aerosol just after releasing the aerosols and two hours after activation.
Figure 4
OH-PLIF results for the CH4 flames. OH-PLIF images 1a–d show OH single-shot images, 1e–h show OH average images of the CH4 flames, and 1i–l show flame cones for re-placing the synthetic air (N2 + O2) by aerosol up to 79 g/m3 just after activating the fire aerosol suppressant while 2a–d show OH single-shot images, 2e–h show OH average images, and 2i–l show flame cones for the similar conditions accomplished two hours after activating the aerosol suppressant. For both cases, the flame condition was at the equivalence ratio, ϕ = 1 and velocity, Vf = 2.5 m/s
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For the experiments performed shortly after releasing the aerosols, both the single-shot and average images clearly show that increasing the amount of aerosol agent significantly reduces the flame cone angle, and thereby the burning velocity. A similar, though much less pronounced, effect is observed in the experiments performed two hours post-activation. Both the reduction in half flame cone angle \(\alpha\) as shown in Eq. 4 [2527], and the extension of the area of the flame reaction zone [2123] imply a reduction in laminar burning velocity. The laminar burning velocity characteristic of different flames and extinguished agents will be discussed thoroughly in the later section. Then the measurements were performed for the highly reactive battery gas mixture. Figure 5 shows OH-PLIF images for the battery vent gas flame when the synthetic air was replaced by aerosol just after releasing the aerosols.
Figure 5
OH-PLIF results for the battery vent gas flames. OH-PLIF images 1a–d show OH single-shot images, 1e–h show OH average images of the battery vent gas flames, and 1i–l show flame cones for replacing the synthetic air (N2 + O2) by aerosol up to 79 g/m3 just after activating the aerosol suppressant while 2a–d show OH single-shot images, 2e–h show OH average images, and 2i–l show flame cones for the same flame conditions for replacing the synthetic air by CO2. The flame condition was at the equivalence ratio, ϕ = 0.7 and velocity, Vf = 5 m/s
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The behavior of the battery vent gas flame was significantly different from that of the CH4 flame when exposed to the aerosol. As the concentration of aerosol (g/m3) increased, the flame cone angle widened, while both the flame length and the reaction zone area decreased. This suggests an increase in the laminar burning velocity. To enhance understanding of the effects of aerosols and H2, two additional sets of experiments were conducted: (a) one with the same battery vent gas flame by injecting CO2 gas, and (b) another with a pure H2 flame by injecting aerosols. The first experiment aimed to clarify the impact of a well-known gas-phase suppressant on the flame by replacing the aerosols with CO2 gas in the battery vent gas flame. The second experiment sought to understand the suppression of pure-H2 flames as well as the effect of H2 molecular diffusivity. According to Fig. 5 2a–l, as the volumetric CO2 gas increased, single-shot and average images indicated that the flame cone angle became smaller, the flame length and reaction zone area extended, and the laminar burning velocity decreased. This observation contrasts with the results for aerosols. Figure 6 shows OH PLIF images for the H2 gas flame when synthetic air was replaced with aerosol immediately after activating the fire extinguisher. The pure H2 flame exhibited similar behavior to the battery vent gas flame, but more significantly. As the aerosol (g/m3) percentage increased, the H2 flame cone angle widened, and the flame length and reaction zone area shrank significantly, resulting in an increased laminar burning velocity.
Figure 6
OH-PLIF results for the H2 flames. OH-PLIF images 1a–d show OH single-shot images, 2a–d show OH average images of the H2 flames, and 3a–d show flame cones for replacing the synthetic air (N2 + O2) by aerosol up to 79 g/m3 just after activating the aerosol suppressant. The flame condition was at the equivalence ratio, ϕ = 0.5 and exit velocity, Vf = 5 m/s
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To summarize the impact of aerosols on the burning velocity of premixed flames simulating a gas explosion, the normalized burning velocities vs injected aerosol concentrations are shown in Fig. 7. The calculations were carried out following the experimental methodology described in Sect. 2.2 and Eq. (1) and the uncertainties (with 95% confidence interval) were calculated based on 199 samples for each condition. Figure 7 indicates that the burning velocity of the battery vent gas and H2 flame exhibits a similar trend with increasing aerosol concentration. Although the burning velocity appears to decrease slightly at lower aerosol concentrations, it increases at higher concentrations. This trend is more significant in the H2 flame as compared to the battery vent gas flame. In contrast, the burning velocity of the CH4 flame consistently decreases with rising aerosol concentration. A similar trend was also observed when increasing CO2 in the battery vent gas flame. The uncertainty was observed to increase with increasing the amount of H2 which is mainly due to the increase in instability in the flame stabilization. As the H2 concentration increased, it became necessary to lower the equivalence ratio (ϕ) to improve stabilization, but some degree of instability remained.
Figure 7
Normalized burning velocity (with a 95% confidence interval uncertainty) for aerosol and CO2 injection in different gas flames
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3.2 Simulation Results

Figure 8 presents laminar burning velocities of premixed flames, over a wide range of equivalence numbers for hydrogen, methane, and the two gas mixtures representing gas from NCA and LFP batteries at 100% charge. The solid lines are without the addition of dipotassium carbonate, and it is clear that there is a very broad range of burning velocities with pure hydrogen burning significantly faster than the other mixtures. The dashed lines represent cases with the addition of a mole fraction of 0.001 dipotassium carbonate, which corresponds to 6.2 g/m3 K2CO3 in the gas mixture. The slow-burning gases methane and the LFP gas mixture are nearly extinguished with this concentration of the extinguishing agent. For pure hydrogen, it is seen that reduction in burning velocity is good in lean mixtures (i.e., mixtures with more oxygen than required for complete combustion), but weak at low oxygen levels. On the NCA gas, at least a reduction in laminar burning velocity of 50% is seen for equivalence numbers up to approximately 1.8, while the fattest mixtures are dampened less effectively.
Figure 8
Laminar burning velocities for the LFP and NCA battery gas mixtures, methane and hydrogen, as a function of equivalence ratio (ϕ) for unperturbed cases and when 6.2 g/m3 K2CO3 is mixed with the gases
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To enable evaluation of the relative efficiency of the aerosol suppressing agent, Fig. 9 presents laminar burning velocities normalized towards the unsuppressed case. The left graph in Fig. 9 shows that the flame suppression is efficient already at low K2CO3 concentrations, for all gas mixtures. However, at stoichiometric conditions, higher concentrations of K2CO3 are needed, in particular for hydrogen. The simulation results indicate that the effect of the flame suppression agent levels out at higher concentrations. Note that the concentration in the simulations refers to the evaporated fraction of the K2CO3.
Figure 9
Simulated laminar burning velocities for the equivalence ratio (ϕ) of 0.7 (left) and 1.0 (right) at a range of concentrations of fire suppressant, normalized towards the property for unsuppressed mixtures
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4 Discussion

The distinct behavior of micro-sized aerosol suppression agents (based on K2CO3) toward H2 and H2-rich battery vent gas flames, specifically, the increase in laminar burning velocity observed in experiments and the discrepancy with simulation results, can be attributed to the phase of the aerosol agents, the properties of H2, and the interaction between the aerosol agents and the H2 flame.
As previously discussed, both thermal and chemical effects can significantly influence flame suppression as aerosol concentration increases. First, these micrometer-sized aerosols absorb heat to initiate evaporation, lowering the flame temperature. Then, they exhibit chemical effects by enhancing recombination reactions and inhibiting chain-branching reactions in the combustion process, leading to successful suppression [12, 30, 31].
For the CH4 flame, the reduction in the flame cone angle and the expansion of the flame reaction zone area, as observed in the OH-PLIF images in Fig. 4, along with the consistent decrease in laminar burning velocity with increasing aerosol concentration shown in Fig. 7, are attributed to the suppressing effects of aerosols. Figure 10 presents a schematic comparing the interaction between (a) aerosol agents and the CH4 flame, and (b) aerosol agents and the H2/battery vent gas flame. The CH4 flame has a low burning velocity, as indicated by previous simulation results, and exhibits significantly high radiative heat transfer (RHT) efficiency due to the presence of CO2, H2O, CO, and possibly soot [32, 33]. The high RHT, combined with extended heat transfer time, promotes the conversion of aerosol agents from solid or liquid to vapor or gas phases in the pre-flame zone, ensuring the effective availability of potassium radicals (K) for gas-phase chemical reactions. The simulation results, assuming complete evaporation of the aerosol, clearly show that K2CO2 has strong flame suppression capabilities through reactions involving various potassium compounds and combustion radicals, primarily OH, H, and O. For lean mixtures, even a concentration of 10 g/m3 of K2CO3 can reduce laminar burning velocities to less than one-third of their original value. These findings for the CH4 flame are fully consistent with the simulation results discussed in Sect. 3.2.
Figure 10
Schematic of the interaction between (a) the aerosol agents and the CH4 flame as well as (b) the aerosol agents and H2/battery vent gas flame
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In the experimental study, however, applying the same suppressing aerosols to the H2 flame or high-reactive battery vent gas flame yielded significantly different results. These differences can be attributed to the high hydrogen content in the fuel mixture and the phase conversion process of the aerosols, from solid/liquid to vapor or gas phase when interacting with the flame. Although the H2 flame burns at a higher temperature than a CH4 flame [34], it is less efficient at radiative heat transfer due to the absence of radiatively active species (e.g., CO2, CO) that are present in methane flame. When aerosols are introduced into a H2-rich flame, local heat loss occurs due to their evaporation. This heat loss is more pronounced in the H2-rich flame compared to a hydrocarbon flame, likely due to its lower radiative heat transfer (RHT) and higher burning velocities [12, 35]. The faster burning rate of the H2 flame reduces the time available for heat transfer to the aerosols in the pre-flame zone. In the flame where no aerosol evaporation occurs, the burning rate remains constant. However, in regions where evaporation takes place, the local cooling reduces the burning velocity, causing different sections of the flame to burn at varying speeds. These instabilities, driven by variations in burning velocity, lead to an increase in the flame area. This explanation can be supported by experiments in spray combustion [36]. In this work by Atzler et al. [36], it was shown that the injection of non-evaporating hollow glass spheres in a laminar gaseous propane–air mixture did not alter the flame surface, which was smooth and similar to that without glass spheres. However, introducing the water aerosol in a gaseous propane/air mixture induced cellular surface structures that initiated instabilities, as compared to the smooth flame in a similar experiment without water aerosol [36]. This work indicates the heat loss from the flame due to the evaporation of water droplets has a significant role in the development of instabilities and cellular surface. Bradley et al. [37] also showed that this cellularity results in an increase in the flame surface area followed by a relative increase in laminar flame. Although previous studies [18] have identified the challenges of evaporating K2CO3 for hydrogen gas mixtures, no indication of an increase in the burning velocity has been identified. This could be due to the significantly larger particle sizes (~ 5 µm), which might reduce heat loss in the flame and result in insufficient formation of cellular structures to increase flame surface area.
As mentioned earlier, the burning velocity for both the battery vent gas and H2 flame decreases slightly at lower aerosol concentrations but increases at higher concentrations. This can be explained by the fact that when the aerosol concentration is sufficiently low, the local heat loss due to aerosol evaporation is not significant. As a result, the suppression effect of the aerosols can dominate and thereby reduce the burning velocity. However, at high aerosol concentrations, significant heat loss occurs due to aerosol evaporation, leading to local cooling. This reduces the local burning velocity, creating instabilities through burning velocity gradients along the flame surface, thereby increasing the flame area and laminar burning velocity. The development of instabilities and cellularity due to heat loss by aerosol evaporation in the flame is connected to the Lewis number, \(Le=\frac{\alpha }{D}\), which is defined by the ratio of thermal (\(\alpha\)) to mass diffusivities \((D)\) of the reactant. Clavin et al. [38] and Harper et al. [39] demonstrated that the Markstein number increases linearly with \(Le\) for a wide range of mixtures. The dimensionless Markstein number (\(Ma\)) characterizes the effect of local heat release of a propagating flame on variations in the surface topology along the flame and the associated local flame front curvature [40]. The larger the Markstein length, the greater the effect of curvature on localized burning velocity. Droplets near the flame front will absorb heat as they evaporate; this reduces the heat diffusion from the reaction zone but is unlikely to change the molecular diffusion. Hence the evaporation process of droplets reduces \(Le\) and, so reduces the \(Ma\) which results in a greater propensity to cellularity [41]. For a larger droplet as compared to smaller ones, the reduction in \(Ma\) is expected to be greater. Besides, due to the rich content of H2 in battery vent gas, the \(Ma\) is also significantly small as compared to as compared to the methane/air flames as H2 has a small Lewis number \((Le=0.3)\) due to having higher molecular diffusivity as compared to thermal diffusivity. Therefore, the investigated battery vent gas is more prone to develop instabilities and so increase in laminar burning velocity as a consequence of heat loss by the aerosol evaporation [42, 43].
For the pure hydrogen flames, shown in Fig. 6, due to preferential diffusion or differences in thermal and molecular diffusion and negative flame stretch, the flame appears open near its tip [44]. If the thermal diffusivity of the premixture sufficiently exceeds the molecular diffusivity (Le > 1) the flame assumes a continuous luminous conical shape. However, in the opposite case, when molecular diffusivity is high enough (Le < 1), the flame appears open near its tip [45, 46]. The unbalance between fuel and oxidant diffusion is known as preferential diffusion. Kozlovsky et al. [47] numerically observed and identified that the Bunsen flame tip opens at mixture conditions having a Lewis number less than unity (Le < 1). Ern et al. [4] investigated the flame structure of lean and rich hydrogen/air, methane/air Bunsen flames to understand the effect of thermal diffusion of the species on the flame structure.
As noted previously, the effects of CO2 gas injection on the battery vent gas flame are quite opposite to those of aerosols. With increasing CO2, the flame cone angle decreases, and the laminar burning velocity drops (see Figs. 5 2a–l and 7). This is because, unlike aerosols, CO2 does not cause heat loss through evaporation, nor does it create local instabilities through burning velocity gradients along the flame surface. Literature [21, 48, 49] suggests that the laminar burning velocity decreases with increasing CO2 concentration. For increasing CO2, the chemical reactivity of the mixture becomes low due to the reduced heat of the flame, which leads to a reduced adiabatic flame temperature and lower concentrations of radicals. High CO2 enhances the recombination reaction of H + O2 + M → HO2 + M, thus reducing the concentration of H radical levels in the flame, affecting the branching reaction H + O2  ↔ O + OH [50, 51]. Therefore, it can exhibit significant local extinction in the reaction zones, affecting the flame's sustainability.

5 Conclusion

Experimental studies, complemented by 1D flame simulations, were performed to understand the effect of K2CO3 aerosols on the flames for a gas mixture mimicking vented gases from an NCA battery2 as well as pure H2.
The simulation study demonstrates a satisfactory extinguishing effect of gasified aerosols; however, aerosol gasification has been identified as a limiting factor from experimental studies in the effectiveness of the extinguishing agent for premixed gas mixtures of highly reactive battery gases (equivalent to NCA at 100% SOC) and hydrogen gas. For those gases, the lower radiative fraction and the higher burning velocity of the hydrogen-rich mixtures, reduce heat transfer to the aerosol in the pre-flame zone, preventing effective evaporation of the aerosols. When the condensed aerosol reaches the flame, it was found to induce a local cooling resulting in a corrugated flame increasing the flame area and thereby the total burning velocity. This is likely to be further enhanced by the preferential diffusion of hydrogen leading to the growth of the cellular structure which should be further investigated.
Less reactive battery gas mixtures (e.g., those associated with lower SOC or less reactive chemistries) were not tested in the current study. However, the results from simulation and experimental studies on CH4 flames indicate that aerosols are more effective for such mixtures. The lower flame burning velocity, combined with higher radiative heat transfer (RHT), facilitates the essential evaporation of the aerosol agent and effectively suppresses the CH4 flame. Similarly, the aerosol suppressant may also be more effective for less reactive battery gas mixtures, but experimental validation is necessary.
In summary, this indicates that, although the aerosol agent has been found highly effective for diffusion flames, a beneficial effect cannot be guaranteed for situations, where a hydrogen-rich gas is allowed to mix with air prior to ignition such as in the case of a gas explosion in gasses emitted from an NCA-battery at 100% SOC or pure hydrogen. To improve the ability of the aerosol to inert gas mixtures with high concentrations of hydrogen, modification of the aerosol such as reduced particle size and higher initial temperature could be considered.

Acknowledgements

The authors would like to thank the company marketing the aerosol for their kind support and approval to publish the results openly.

Declarations

Conflict of interest

The authors declare that they have no conflict of interest.
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Titel
On the Effectiveness of Aerosol Extinguishing Agents for Battery Vent Gases and Hydrogen
Verfasst von
Arman Ahamed Subash
Elna J. K. Nilsson
Marcus Runefors
Publikationsdatum
16.01.2025
Verlag
Springer US
Erschienen in
Fire Technology / Ausgabe 6/2025
Print ISSN: 0015-2684
Elektronische ISSN: 1572-8099
DOI
https://doi.org/10.1007/s10694-024-01691-w
1
Experiments with a mixture mimicking LFP were attempted, but, due to heat loss to the burner rig, no stable flame was achieved and, therefore, the LFP-mixture was only used in the simulation study.
 
2
Experiments with a mixture mimicking LFP were attempted, but, due to heat loss to the burner rig, no stable flame was achieved and, therefore, the LFP-mixture was only used in the simulation study.
 
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