Thermal localization leads to reaction initiation in granular materials. Observations show that it occurs in the vicinity of large pores and, thus, depends on a material's microstructure. Since the spatial variability of the latter cannot be ascertained in all its relevant details, we treat the material's initial porosity as a random field. The so-called “hotspots” are then modeled as rare events in a complex nonlinear dynamical system. Their probability of occurrence is quantified by the tails of the distributions of the temperature and the corresponding reaction rate. These are computed via Monte Carlo simulations of a two-phase five-equation dynamic compaction model, which are supplemented with a mesoscale model of the thermal localization at the solid-gas interface. Our results demonstrate a strong nonlinear dependence of the probability of hotspot initiation on the variance of the initial porosity.

Granular compaction has many important applications including processing pharmaceutical tablets,1 metal powder consolidation,2 diamond synthesis,3 and energetic materials safety.4 The behavior of reactive granular materials under dynamic compaction has been the subject of numerous experimental and theoretical studies.5–8 The added complexity in understanding reactive powder mixtures lies in the need to model and predict thermal localization in critical areas of the material, known as “hotspots,” where ignition occurs.

Although the physics of hotspots is not yet fully understood,9 observations confirm the hypothesis that reaction initiation occurs in the vicinity of macropores.10 This is consistent with the fact that areas with high plastic deformations cause large thermal dissipation and consequently extreme temperature fluctuations, which trigger chemical reactions. Other dynamic phenomena, such as shear banding11 and elastoplastic deformation concentration due to material heterogeneities,9 are also likely mechanisms contributing to hotspot formation. Furthermore, the grain size distribution has been shown to play a major role in the sensitivity of hotspot formation.4 

In light of this knowledge, phenomenological12 and computational9 models of reaction initiation have been developed. The most common modeling approach is to use continuum models with thermodynamic closures and equations of state that are consistent with physics. Such continuum models account only for averaged microscopic dynamics, ignoring localization events that are due to microstructural defects. Since accurate physical measurements of reaction initiation are elusive, one has to rely on numerical modeling and simulation to study hotspot formation.

Hotspot formation in energetic materials has been extensively analyzed using (i) molecular dynamics simulations studying the thermochemical properties of hotspot formation, (ii) mesoscale pore collapse models of either a single pore or a few microstructural defects, characterizing the effect of the pore size and morphology on reaction initiation, and (iii) multiscale models that combine microscale dynamics with continuum models.

Molecular dynamic simulations13,14 are essential to understand the underlying chemistry of hotspot formation. Yet, their computational cost renders them impractical for making quantitative predictions at the device scale.

Pore-scale numerical simulations have been used to characterize the criticality of hotspot formation.10,15–17 The early work on isotropic (i.e., one-dimensional/radial) compaction of a viscoplastic spherical shell18,19 has been extended to two- and three-dimensional simulations of a single macropore collapse.15,20,21

Multiscale simulations incorporate this mesoscale dynamics into continuum models by adding source terms, such as the phase pressure difference8 or a reaction rate model,22 to the latter. Another multiscale approach23 is to build a surrogate model from multiple mesoscale pore collapse simulations and use it as part of a continuum scale simulation.

While the current trend in modeling hotspot formation is to incorporate as much physics as possible, the predictive uncertainty of the resulting models (on any scale) is largely ignored. Specifically, continuum models are largely phenomenological and often neglect the subscale dynamics that is believed to be essential for hotspot formation. At any scale, models involve unknown parameters that are adjusted to fit experimental data, without necessarily reflecting the underlying physics. Although there is consensus that hotspots cause reaction initiation, they occur over wide time scales (10–5–10–3 s), space scales (≈0.1–10 μm), and temperature ranges (≥700 K).24 This makes it impossible to obtain accurate measurements and reliably validate a physical hypothesis. Consequently, many questions about modeling assumptions remain unanswered.

Is a single solid phase viscoplastic Euler model accurate enough to model granular compaction,22,25 or is the gas phase essential for capturing the dynamics of hotspot formation?26 Do closure terms in the two-phase models honor the underlying physics? Are equilibrium thermodynamic assumptions appropriate in a physical problem that is (clearly) very far from equilibrium? How accurate is the nonconservative compaction law in, e.g., the Baer-Nunziato model? Is the atomistic scale relevant in studying hotspot formation?

The absence of direct observational data does not allow one to discriminate between alternative modeling hypotheses and, hence, to answer conclusively these basic questions. For instance, two models might predict different temperatures and reaction rates, but be equivalent within a range of irreducible uncertainties. Thus, increasing modeling complexity and improving numerical accuracy do not necessarily improve the predictive power when the model parameters are uncertain.27 

Yet, most material properties, e.g., porosity, pore size distribution, and heat capacity, are heterogeneous, and their point values are knowable only probabilistically. The values of some characteristics, such as viscosity and yield strength, are up to 100% uncertain in energetic materials like HMX.9 Solid surface properties are usually assumed the same across the solid-gas interface, often without experimental validation.

These ubiquitous structural (model) and parametric uncertainties argue for the use of Occam's razor: A model that honors experimental observations with the fewest modeling assumptions is preferable. Guided by this principle, we show that treating initial porosity as random is sufficient to capture hotspot formation using a standard continuum model described below. The Monte Carlo solution of this problem reveals the high sensitivity of the probability of reaction initiation to the heterogeneity of initial porosity, which is consistent with experimental observations.

Two-phase (solid/gas) flow models5,28 are widely used to describe the dynamics of a granular material under dynamic compaction (Fig. 1). In their original formulation, these seven-equation models combine conservation laws for mass, momentum, and energy in each phase with a nonconservative compaction equation for the volume fraction.5 Subsequent studies provide simplified and regularized versions of the Baer-Nunziato equations,6,29 found the relevant equations of state,30–32 and added terms (e.g., “configurational stress”) to account for the granular microstructure.4,28 Despite their usefulness, these equations are known to be numerically unstable.

FIG. 1.

Dynamic compaction of a granular material.

FIG. 1.

Dynamic compaction of a granular material.

Close modal

A single velocity/single pressure approximation6 regularizes the equations and reduces the numerical instability.33 The pressure-equilibrium assumption implies that the interface between the two phases is large. This five-equation model assumes the solid and gas phases to have the same velocity u and pressure p, giving rise to four conservation equations

(1a)
(1b)
(1c)
(1d)

where the subscripts s and g stand for the solid and gas phases whose densities are ρi (i = s and g) and volume fractions are αi (i = s and g). The solid-gas mixture has density ρ=αsρs+αgρg, internal energy e=αsρses+αgρgeg (with es and eg denoting the internal energy of the solid and gas phases, respectively), total energy E=e+Bs(αs)+u2/2 (with Bs denoting the configuration energy, a prescribed function of αs, and the granular or configuration pressure defined by βs=αsρsdBs/dαs), and pressure p=αsps+αspg+βs supplemented with the stiffened gas equation of state for the i-th phase pi=(γi1)ρieiγipi,, where γi and pi, are known material dependent constants. The fifth equation comprising the model is a nonconservative compaction law

(1e)

Hotspots are believed to occur in large pores where heat dissipation due to large plastic deformations and friction is the highest.34 Therefore, the main quantity of interest (QoI) is the temperature at the solid/gas interface, rather than the average temperature T¯(x,t) that can be deduced from the internal energy of the continuum model (1). The mesoscale temperature, Tμ, is governed by a reaction-diffusion equation

(2)

The Laplacian κ2Tμ represents heat conduction into the solid bulk material. The rate of dissipation due to friction and permanent plastic deformation, Q̇D, is, e.g., given by the deformation power.19 The exothermal reaction heat generation term, Q̇R, follows an Arrhenius law.12,22 In our analysis of hotspot formation, we focus on the dynamics before the onset of chemical reactions and neglect the reaction dissipation term Q̇R.

Our QoI is the pore-surface temperature Tps(x,t)=Tμ(xsg,t), where xsg is a point on the solid-gas interface. We expect that TpsT¯, which can significantly change predictions of hotspot formation based on the continuum scale model. To account for the discrepancy between the continuum- and pore-scale temperatures, we adopt a reduced-order mesoscale heat model.8 This model redistributes the macroscale temperature T¯(x,t) across the granular matrix by assuming a spherical shell mesoscale representation of the pores (Fig. 2).

FIG. 2.

Mesoscale spherical pore heat model.

FIG. 2.

Mesoscale spherical pore heat model.

Close modal

The heat generated at the pore surface, qc, depends on plastic deformation and, thus, on the rate of decrease in porosity αg/t. For spherical pores, αg=43πRg3Ng, where Rg is the pore radius and Ng is the number of pores per unit volume. The heat generated at the surface dissipates into the bulk of the solid phase by heat conduction, qs. The resulting temperature profile is given by the solution of the diffusion equation over a spherical shell. This gives the pore surface temperature8 

(3)

where λs is the thermal conductivity and the parameter n determines the shape of the temperature profile. The heat dissipation boundary layer δ is determined from the average temperature constraint T¯=1/VRgδTdV (Fig. 2). The core temperature Tcore is determined from the solid-phase Hugoniot relation

where νs=1/ρs and the superscript 0 denotes the preshocked state.

An alternate measure of the probability of reaction initiation is the reaction rate Ṙ related to the pore surface temperature Tps via the Arrhenius rate law4 

(4)

where the exponential prefactor Z and the activation temperature T* are known for a given material; they are set to Z =5 × 10–19 s−1 and T* = 2.65 × 104 K in our simulations.4 In this study, this quantity measures the “potential” average number of reactions triggered per unit time, without actually having reactions to take place. This assumes that the expected number of reactions per unit time is directly related to the probability of initiation at each point (x, t).

Microstructural heterogeneity in granular materials is the source of (i) fast temperature and stress fluctuations in the vicinity of large pores and (ii) an epistemic uncertainty in the key pore size and material property distribution. Accordingly, we treat the initial porosity, αg(x,t=0), as a spatially uncorrelated Gaussian random field, αg(x,0)N(α¯g,σg2), such that

(5)

where · denotes the ensemble average. This approximation is valid for randomly packed grains with no spatial correlation at the grid size (∼10 μm). Spatially correlated microstructures inferred from real images can also be used.

We use (1)(3), subject to this random initial condition, to estimate the probability of pore-surface temperature Tps(x,t) exceeding a reaction initiation threshold Tig

(6)

where FTps is the cumulative distribution function (CDF) of the random surface temperature Tps(x,t). We start by assuming that reactions are instantaneously triggered when Tps exceeds the known threshold Tig, which represents a zeroth-order approximation of the probability of reaction initiation.

We use Monte Carlo simulations to estimate these probabilities. In every realization, (1)(3) are solved with the initial condition αg(x,0) drawn from the distribution N(α¯g,σg2) at every grid-point with no spatial correlation. The simulation domain of length 1.6 cm is discretized with 200 grid points, and Nr = 600 realizations were performed. Every realization i yields a pore-surface temperature Tpsi(x,t). The ensemble average is approximated by the sample average TpsTpss=iTpsi/Nr, and the probability density function is constructed using a kernel density estimator fTps(T̂;x,t)iKh(T̂Tpsi(x,t))/Nr, where T̂ is a sample space variable and Kh(·) is a Gaussian kernel with bandwidth h.

A Godunov-type HLLC numerical scheme33 is used, with a velocity boundary condition, vp60 m/s, on the left boundary (Fig. 1) and a reflecting boundary condition on the right (although the simulation is stopped right before the shock reaches that boundary). The nonconservative and highly nonlinear nature of the compaction law (1e) requires special treatment to preserve the volume fraction positivity.

Figure 3 shows a snapshot of one realization of the two main variables at time t =12 μs: the solid volume fraction αs(x,·) and the pore surface temperature Tps(x,·). The temperature is higher, particularly at the shock front, for a higher microstructural heterogeneity corresponding to a larger σg. Comparison of the gas volume fraction before and after the shock reveals that once the grains are compressed, the porosity becomes relatively homogeneous. Hence, larger pores deform more than smaller ones, thus dissipating more energy. This is consistent with experimental observations.9 

FIG. 3.

Spatial profiles of the solid volume fraction αs (left) and pore-surface temperature Tps (right) at time t =34 μs, for two values of the microstructural fluctuation strength σg.

FIG. 3.

Spatial profiles of the solid volume fraction αs (left) and pore-surface temperature Tps (right) at time t =34 μs, for two values of the microstructural fluctuation strength σg.

Close modal

The average pore-surface temperature Tpss is almost independent of the initial microstructural heterogeneity σg (Fig. 4, left). However, the average reaction rate Ṙs increases with σg (Fig. 4, right). The increased sensitivity of Ṙs to σg is due to the nonlinearity of the Arrhenius law, which gives exponentially higher weights to higher temperatures.

FIG. 4.

Average temperature (right) and the corresponding reaction rate (left) as a function of microstructural heterogeneity σg.

FIG. 4.

Average temperature (right) and the corresponding reaction rate (left) as a function of microstructural heterogeneity σg.

Close modal

Both the average pore-surface temperature Tps(x,t)s and the average reaction rate Ṙs are the highest along the line x/t=vsh, where vsh is the speed of the shock (Fig. 5). This is because the highest rate of thermal generation occurs where the change in porosity is the highest. Behind the shock front, the temperature decreases due to thermal diffusion in the bulk.

FIG. 5.

Average reaction rate Ṙs (left) and average pore-surface temperature Tpss (right), for the coefficient of variation σ¯g=0.0375.

FIG. 5.

Average reaction rate Ṙs (left) and average pore-surface temperature Tpss (right), for the coefficient of variation σ¯g=0.0375.

Close modal

Figure 5 shows the average reaction rate and pore surface temperature. The line with the peak reaction rate and pore surface temperature coincides with the shock front where plastic deformations are the highest. The average temperature behind the shock front is higher than the initial temperature due to the increase in pressure after compaction (also see Fig. 3). Temperature fluctuations cause the reaction rate to grow exponentially due to the Arrhenius law. This explains the fluctuations in the sample mean of the reaction rate, which amplify rare extreme temperature fluctuations that are averaged out in Tpss. The impact of the increase in temperature behind the shock front is insignificant compared to that of extreme fluctuations.

We posit that the reaction initiation occurs when the temperature Tps exceeds a certain threshold Tig and computing the probability of this event, P[Tps(x,t)>Tig] using (6). This probability is shown in Fig. 6 as a function of Tig (left) and σ¯g (right), for an arbitrary point (xh, th) along the shock front (chosen for illustration). This observation highlights the fact that hotspots are not a function of the average pore surface temperature, but of the tail of the distribution. Furthermore, the dependence on Tig confirms the intuition that the probability of initiation increases as the ignition threshold is lowered, thus becoming easier to exceed.

FIG. 6.

CDF of a random pore-surface temperature Tps at a given point along the shock front (xh, th) (left). Probability of reaction initiation as a function of the strength of microstructural fluctuations σg for different ignition temperatures Tig (right).

FIG. 6.

CDF of a random pore-surface temperature Tps at a given point along the shock front (xh, th) (left). Probability of reaction initiation as a function of the strength of microstructural fluctuations σg for different ignition temperatures Tig (right).

Close modal

The exceedance probability in Fig. 6 provides a partial description of the probability of reaction initiation. Another relevant statistics is the probability of Tps remaining above the ignition threshold Tig for a certain time interval τ=t2t1 that is sufficient for the reactions to take hold. In other words, we are concerned with the probability of Tps>Tig during a given time interval τ: P[Tps(x,t1)>Tig,Tps(x,t2)>Tig]=Ft[τ|Tps>Tig], for all x and all permutations of t1 and t2. The corresponding CDF in Fig. 7 shows that the time interval during which temperature Tps remains above the threshold Tig increases with the microstructural fluctuation coefficient of variation σ¯g.

FIG. 7.

Probability density function of the time spent above the reaction initiation threshold, for a 34 μs simulation.

FIG. 7.

Probability density function of the time spent above the reaction initiation threshold, for a 34 μs simulation.

Close modal

In summary, we demonstrated the dependence of reaction initiation in compacted granular materials on the initial pore size distribution using a fluctuating initial microstructure. Our results show that the amplitude of the fluctuations in the initial porosity affected the distribution of the resulting pore-surface temperature, motivating a probabilistic approach to studying hotspot formation. The corresponding reaction rate and probability of initiation are sensitive to the fluctuation amplitude. This study demonstrates that a probabilistic approach is the simplest and most intuitive way to study reaction initiation in granular materials, given a fundamentally uncertain and spatially heterogeneous material microstructure.

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