# From episodic avalanching to continuous flow in a granular drum

- 134 Downloads

## Abstract

Experiments are conducted to study the transition from episodic avalanching (slumping) to continuous flow (rolling) in drums half full of granular material. The width and radius of the drum is varied and different granular materials are used, ranging from glass spheres with different radii to irregularly shaped sand. Image processing is performed in real time to extract relatively long time series of the surface slope derived from a linear fit to the granular surface. For the drums with glass spheres, the transition mostly takes the form of a blend of the characteristics of episodic avalanching and continuous flow, that gradually switches from slumping to rolling as the rotation rate increases. For sand, a hysteretic transition can be observed in which one observes prolonged episodic avalanching or continuous flow at the same rotation rate, spanning a window of rotation speeds. For drums with the smallest spheres (1 mm diameter), the transition takes the form of noise-driven intermittent switching between clearly identifiable phases of episodic avalanching or continuous flow. This style of transition is also found for the sand in either the largest or smallest drum (by volume). We formulate dimensionless groupings of the experimental parameters to locate the transition and characterize the mean surface slope and its fluctuations. We extract statistics for episodic avalanching, including angle distributions for avalanche initiation and cessation, the correlations between successive collapses, mean avalanche profiles and durations, and characteristic frequencies and spectra.

## Keywords

Granular media Rotating drum Granular avalanche## 1 Introduction

The flow of grains in a horizontally rotating drum is one of the simplest experiments to perform, yet exemplifies most of the key features that complicate the dynamics of a granular medium [4, 27]: as the drum rotates, phases of solid-like behavior can co-exist with liquid-like or gas-like phases or be transformed into them. Even when the mean flow field is steady, particles can traverse yield surfaces to become entrained into flow or deposited into a solid bed. Finally, flow can abruptly halt or begin to furnish extensive intermittent motion. Thus, the rotating drum is perhaps the archetypal granular experiment. However, despite decades of study, most aspects of drum flow cannot be explained by any one model. For example, continuum models based on empirical friction laws [13] or kinetic theory [18] chiefly apply to steady or rapid flow conditions and have had some success in applications to rotating drums (e.g. [15, 20, 29, 30]). Nevertheless, the models do not describe all the dynamics when there are unsteady transitions from solid-like to fluid-like behavior. Worse, the literature on drum dynamics contains a number of overly simplistic or inaccurate theories and a variety of conflicting observations and interpretations, painting a poorly quantified picture of one of the more fundamental granular flow configurations. A first step to remedy this situation is to obtain reliable, reproducible and accurate experimental data, exploiting the continuous operation and image processing ability of modern cameras and computers to generate long stationary time series and high-quality statistics, which is one of our current goals.

For a roughened cylinder, for which the granular material is unable to slide freely over the container, the low-speed flows are popularly classified as either “slumping” or “rolling” [16, 27]. The former consists of intervals of solid-body rotation that are interrupted by episodic avalanches and arises at the lowest rotation rates. The continuous steady flow of the rolling state emerges at higher rotation speeds. For both slumping and rolling, the granular surface often remains relatively flat and is well characterized by a “dynamic friction angle”; there is only ever a shallow superficial flowing layer, bordered from the rigidly rotating grains below by a yield surface. At yet higher rotation rates, the surface profile becomes nonlinear, with a characteristic S-shape; eventually, rapid, gas-like flow emerges associated with significant centrifuging.

The transition between episodic avalanching and continuous flow has been documented to depend on particle diameter (relative to drum diameter) and shape, the aspect ratio and fill fraction of the drum, effective gravity and degree of cohesion [3, 8, 16, 24, 25, 36]. Several studies have attempted to qualitatively describe the transition in terms of the matching of two distinct timescales. For example, it has been argued [17, 27] that the transition occurs when the typical duration of an avalanche matches the time taken for the same amount of material to rotate rigidly through a comparable angular change. This criterion has some empirical support, as do some other qualitative criteria [8, 23, 32, 34]. However, none of these conditions emerge as the prediction of a dynamical theoretical model, nor do these studies address the precise form of the transition as a bifurcation in dynamical behavior. Indeed, experimental studies often report a “transitional regime,” with mixed characteristics of both slumping and rolling, but offer no quantitative details (e.g. [3, 7, 16]).

By contrast, it has also been stated that the transition has a hysteretic form [32]: as one increases the drum rotation rate, episodic avalanching persists up to a threshold, before switching abruptly to continuous flow. If one then lowers the rotation rate, the continuous flow regime only becomes interrupted by episodic avalanching at a second, somewhat lower threshold. Both flow states are possible over the window of rotation rates sandwiched between the two thresholds. This description is rather different from a dynamical melange of slumping and rolling.

A third perspective suggests that the transition is noise-driven, and detailed experimental observations indicate a “bifurcation by intermittency” [12]. In this scenario, there are again two co-existing states, but noise disrupts episodic avalanching at the higher rotation rates and terminates continuous flow at low speeds. Over the window of the transition, the two states remain distinct and clearly identifiable, but stochastic fluctuations prompt intermittent switches between them. It is not clear whether the mix of behavior reported in other studies corresponds to this intermittent switching, or whether the system dynamics was rougher, with no clear division into recognizable prolonged states of episodic avalanching or continuous flow.

A complementary theoretical approach is based on modeling the avalanching granular medium as a fluid-like continuum accelerating under gravity but retarded by solid-like friction [4, 33]. The crudest models describe the dynamics in terms of a single evolution equation for the surface angle \(\theta (t)\), allowing for switches in flow in the manner of a granular stick-slip friction law [28]. When static friction is higher than dynamic friction at the initiation of flow, and if the latter then increases with flow rate (as in traditional Bagnold-type friction laws), the models predict two possible flow states at low rotation rates: a periodic stick-slip-type motion reproducing the episodic avalanching state, and a steady state representing continuous flow. As one increases the rotation rate, the periodic stick-slip solution eventually disappears in a deterministic bifurcation, with the system then converging to the rolling state. The critical rotation rate at which the periodic oscillations disappear offers a rationalization of the transition from slumping to rolling. Moreover, the presence of two co-existing states at lower rotation speeds implies pronounced hysteresis. However, the continuous flow state exists for arbitrarily low rotation rates and there is no transition from rolling to slumping. This can be remedied by destabilizing the steady state in another deterministic bifurcation at low rotation rates by forcing the friction to start decreasing with flow speed [4, 33]. Alternatively, noise can be added to the model to account for fluctuations due to the finite-size, granular nature of the medium. The continuous flow state is then disrupted at lower rotation rate and episodic avalanching at higher rotation rates without passing through any deterministic bifurcations, and the system can progress from one with pronounced hysteresis to one having an intermittent transition by raising the noise level [12].

Dimensions of the drums, their ranges of rotation rate, and the particle diameters and characteristic angles of the granular materials

Drum diameter (inner), | 287, 190, 152, 100 | 137 | ||

Drum widths, | 17, 31, 56, 110, 205 | 17, 31, 56, 86 | ||

Rotation rates, \(\varOmega \,\mathrm {rad}\,\mathrm{s}^{-1}\) | 0.004–1 | 0.01–1 |

Nominal particle diameter (mm) | Range (\(\mu \)m) | \(\theta _{1}\) | \(\langle \theta _{\mathrm {start}}\rangle \pm \sigma _{start}\) | \(\langle \theta _{\mathrm {stop}}\rangle \pm \sigma _{stop}\) |
---|---|---|---|---|

| ||||

1 | 783–1132 | 21.3 | \(21.7\pm 0.1\) | \(20.9\pm 0.1\) |

1.5 | 994–1483 | 24.7 | \(25.4\pm 0.3\) | \(24.3\pm 0.2\) |

2 | 1800–2200 | 25.4 | \(26.1\pm 0.3\) | \(24.9\pm 0.2\) |

3 | 2800–3200 | 26.5 | \(27.6\pm 0.4\) | \(25.8\pm 0.3\) |

5 | 4800–5200 | 28.0 | \(29.8\pm 0.7\) | \(26.9\pm 0.5\) |

10 | 9800–10300 | 30.5 | \(33.7\pm 1.4\) | \(28.3\pm 1.2\) |

16 | 15600–16500 | 33.4 | \(37.7\pm 2.0\) | \(30.1\pm 1.6\) |

| ||||

1 | 624–1335 | 36 | \(38.7\pm 0.3\) | \(34.8\pm 0.4\) |

## 2 The experiment

### 2.1 Apparatus

Our experiments were conducted using drums made from two acrylic cylinders fitted with a transparent front plate and a paper-covered back wall. For each, the position of the back wall could be adjusted to vary the drum width *W* (axial length), and the inner cylindrical surface was covered with (60 grit) sandpaper to reduce any slip of the granular materials. Most of the experiments were conducted in the larger of the cylinders, with a diameter \(D=287\) mm, which was rotated relatively precisely at a prescribed rate using friction rollers driven by a computer-controlled motor (see Appendix A). The front plate was made from glass. Cylindrical inserts with centering spacers were fabricated so that the diameter could be changed whilst using the same driving apparatus and data acquisition system. The smaller cylinder, with a diameter of about 137 mm, had an acrylic front face and was mounted co-axially on a shaft driven directly by a geared-down motor. This second cylinder was used for a smaller number of more detailed measurements of the avalanching granular surface. The dimensions of the drums are provided in Table 1.

To eliminate one of the experimental parameters, in all experiments the drum was half filled with the granular media (the “fill fraction” was 0.5). We used glass spheres for the most part, with the range of diameters listed in Table 1. We also used a poly-disperse sand with a mean diameter of about a millimeter. Table 1 reports some characteristic friction angles for these materials. It is conventional to determine such angles by building sandpiles or tilting a plane layer. However, the statistics for surface slopes are far better measured in the rotating drum. For example, in the episodic avalanching regime at low rotation speed, we can extract satisfying statistics for the angles at which avalanching begins (\(\theta _{\mathrm {start}}\)) and ends (\(\theta _{\mathrm {stop}}\)). These quantities are random-looking variables with well-defined distributions; our measurements determine the mean values far more precisely than a sandpile experiment. One awkward issue is that the angles depend on drum width *W* and diameter *D* in our experiments (Sects. 3.4, 3.5); Table 1 quotes results for a relatively large drum with \(D=287\) mm and \(W=110\) mm, for which at least the effect of the side walls is minimized. Mean angles of this type are also sensitive to ambient noise, dust and humidity. Indeed, a disturbing feature documented presently (Sect. 2.3) is a persistent ageing effect that leads to secular drifts of these angles as the drums rotate over long periods. Overall, despite their simple appeal, mean angle measurements of this sort are not robust measures of granular dynamics. We did not attempt to calibrate an empirical friction law like “\(\mu (I)\)” using sheet flow down an inclined plane [14] (see also Appendix B).

The experiments were conducted in air-conditioned laboratories; the humidity was monitored to be \(50\pm 10\%\) over their duration. Although the humidity was not precisely controlled, once the granular materials were loaded inside the drums, the arrangement was well sealed and so humidity was unlikely to vary during each suite of experiments (i.e. the up-down sweeps described in Sect. 2.3). Nevertheless, humidity effects may have influenced the dynamics of some of smaller particles we used (1 mm glass spheres and the sand). The big drum was fixed to an optical table set on a workbench and included vibration shielding. The smaller drum was mounted on a heavy wooden board. No further effort was made to reduce ambient noise, with other devices in the laboratory in operation during the experiments.

### 2.2 Data analysis

For each rotation rate, we used a machine vision camera, directly connected to a computer, to observe images of the granular medium through the front face of the drum. With a sampling rate of twenty or fewer frames per second, the images could be processed in real time, thereby avoiding the post-processing of excessive amounts of stored data. In particular, we used the contrast between the relatively bright particles and the back (matt black paper covered) wall to extract the location of the granular surface (defined by the upper edges of the top layer of grains) near the front glass face over a central section of the drum spanning about nine tenths of the total surface. The time series of the dynamical friction angle, \(\theta (t)\), was then recorded exploiting a linear fit to the surface profile. Further details of the fitting process are summarized in Appendix A. For the 137 mm drum, we recorded movies of shorter duration and extracted the surface profile as a function of space and time.

For episodic avalanching, we record the starting and stopping angles of each collapse, \(\theta _{\mathrm {start}}\) and \(\theta _{\mathrm {stop}}\), and the avalanche “amplitude” \(\varDelta \theta =\theta _{\mathrm {start}}-\theta _{\mathrm {stop}}\). Practically, the angles are determined by detecting all the local extrema in the time series that are separated in time and amplitude by preset thresholds. The thresholding artificially deletes some of the smaller avalanches from the record; we chose the thresholds to be as small as possible to avoid such deletions but avoid the false detection of events due to noise in the signal (cf. Appendix A). The procedure records data during the rolling regime, which do not correspond to “starting” and “stopping” angles. These measurements can still be useful as they provide another diagnostic of the fluctuations during continuous flow. In fact, for all our experiments, \(\langle \varDelta \theta \rangle \) was closely related to \(\sigma \).

### 2.3 Burn-in

To explore the transition from episodic avalanching to continuous flow, we performed sequences of experiments corresponding to sweeps of rotation rate \(\varOmega \), holding fixed the other experimental parameters. For each sweep, \(\varOmega \) was incrementally raised and then lowered, waiting at each rotation rate for well over a hundred episodic avalanches or particle circulations during continuous flow. At all but the very lowest speeds the drum made at least one complete rotation. Short sections at the beginning of each time series were deleted to remove transient adjustments occurring after the rotation rate was stepped up or down.

At the outset of our exploration, a pronounced ageing effect became evident that made the sweeps problematic to conduct. The ageing corresponded to a gradual systematic drift in the mean surface angle, \(\langle \theta \rangle \), that we attribute to a combination of accrued damage to the surfaces of the particles and the associated generation of fine dust (secular drifts of surface slope have also been observed to occur due to the cohesive action of humidity, but typically for smaller particles than those used here [1]). For the bigger particles, the surface damage and dust were visible to the eye (for \(d=16\) mm, the damage was substantial, leading us to limit our use of this material); for the smaller particles, the damage was much less noticeable, even under a microscope. Sample secular changes during repeated up-down sweeps with \(d=3\) mm glass spheres are shown in Fig. 1. Progressing from sweep to sweep, the mean angles drift to higher values; the net change is dramatic, exceeding a degree.

For the larger glass spheres and sand, even though the mean angle drifted during the repeated sweeps, the other statistical measures of the signal, \(\sigma \), \(\langle \varDelta \theta \rangle =\langle \theta _{\mathrm {start}}-\theta _{\mathrm {stop}}\rangle \) and \(D_{skew}\), showed little or no such trend; see Fig. 1b–d. Thus, despite the drift, other key features of the drum dynamics were robust, including the rotation rates characterizing the transition between slumping and rolling. The transition, occurring for rotation rates near \(\varOmega \approx 2\times 10^{-4}\,\mathrm {rad}\,\mathrm{s}^{-1}\) in the figure, is detected by the sharp change the diagnostics plotted in panels b–d. By contrast, for the smaller spheres with \(d\le 1.5\) mm, the mean angle drifted to smaller values as the material aged and all the statistical measures also changed, with the rotation rates marking the transition shifting to lower values as the sweeps progressed. Most disconcertingly, after two up-down sweeps, the transition had migrated to such low rotation rate that episodic avalanching could barely be observed (see Fig. 30 in the Appendix; hereon, we cite such figures using the superscript notation “\(^{\circledS }\)”).

The drift of the mean angle could also be observed if the drum was rotated steadily at relatively high speed (0.4 rad/s). In such experiments, the drift largely subsided after a characteristic “burn-in” time for all the particles\(^{\circledS 31}\). This feature provided a convenient protocol for maturing particles to remove the problematic drift: starting with a fresh sample of particles, we first rotated the drum at constant, relatively high speed (\(\varOmega =0.4\,\mathrm {rad}\,\mathrm{s}^{-1}\)), monitoring the mean angle. Once any drift had subsided (which usually required many hours), we terminated this preliminary “burn-in” experiment and then conducted the up-down sweep in rotation rate. This ensured that there was minimal secular change between the rising and falling parts of the sweep, enabling us to look unambiguously for any other forms of hysteresis. Results from two sweeps with different batches of matured 3 mm spheres are included in Fig. 1; the elimination of the secular drift leaves discrepancies of order 0.1 degrees between the two batches that we attribute to basic experimental error (slight differences in the fill fraction of the drum, the fit of the surface slope, camera or drum positioning and so forth).

To avoid repeating excessively long burn-in runs, we also recycled matured particles. In particular, we first matured particles in the drum with \((D,W)=(287,110)\) mm, and then used the matured batches for all the subsequent sweeps in drums with different width and radius. The recycled material still required some degree of burn-in (due perhaps to the loss of dust during removal and refilling of the drum), but typically less than half the time. The sandpaper lining the drums was also worn down by conducting repeated sweeps; we replaced the lining whenever wear became noticeable. No appreciable wear of the glass face of the big drum was discernible (the smaller drum was not used for sufficient time to wear the acrylic face.)

## 3 The results for glass spheres

### 3.1 Phenomenology

The transition for the smallest particles (\(d=1\) mm) took a clearer form, with intermittent switching between clearly identifiable periods of episodic avalanching and continuous flow; see Fig. 3. As the rotation rate increased through the transition, the typical residence time in episodic avalanching gradually dwindled until that state was replaced by uninterrupted continuous flow. Thus, for \(d=1\) mm the transition has a clear intermittent character [12], with the residence time in the two phases providing a diagnostic of the transition. For the rest of the spheres, the dynamics more effectively blended the features of the two states, rendering a residence time diagnostic difficult to extract.

### 3.2 Sweeps

Up-down sweeps of the glass spheres for different particle radius and drum geometry are shown in Fig. 5; the gradual transition between episodic avalanching and continuous flow leads to a smooth connection between \(\varOmega -\)independent statistics for low rotations rates to more systematic variations at higher speeds. Figure 5a shows data for the drum with \((D,W)=(287,110)\) mm, and varying particle diameter *d*. Fig. 5b, c show data for 3 mm spheres in drums with different diameter *D* and width *W*, respectively. The figures illustrate how the rotation rates for transition vary significantly with *D* and *d*, but not with *W*. Both the mean angle and its variability depend significantly on all of *D*, *W* and *d*. In this figure, and in subsequent figures, each data point is an average over all experiments with the same parameters \((\varOmega ,d,D,W)\).

*W*once the drum is sufficiently wide. Such width-independent behavior appears roughly for \(W>\frac{1}{3}D\), independently of particle diameter and shape (being similar for all the glass spheres and sand), and in agreement with previously presented data [5]. Many of the experimental drums used in previous studies are relatively narrow according to this criterion, with mean angles that are controlled by the side walls [3, 10, 30]. Despite this, the apparent independence of the flowing layer depth on

*W*as observed through the side wall is sometimes taken as evidence for width-independent dynamics. Although we did not directly measure this depth, it was apparent from our image statistics (specifically, the mean difference between consecutive images, which highlights flowing rather than rigidly rotating particles) that the flowing layer also did not vary significantly with

*W*at the front face of our drums. The situation is presumably similar to heap flows in a slot, for which it is argued that sidewall friction always controls the flowing layer depth and increases with

*W*until the slot width becomes comparable to the length of the apparatus [19]. Thus, observations through the sidewall must be biased, with the flowing layer being much deeper than can be seen, as has been verified in NMR experiments [26].

Measuring mean angles through the front face of the drum can also be problematic, as surface slopes vary with axial position. For glass spheres, it has been reported that the surface angle changes by as much as \(4^\circ \), with material piled up higher against the front and back walls [9]. By itself, this variation is not sufficient to explain the differences in mean angle for different *W* observed for our drums (Fig. 5c). The characteristic range of the boundary effect is reported to be of the order of 0.14*D*, provided the particles are not too large. This suggests that the front and back wall are effectively isolated from one another when \(W>0.28D\), in agreement with our rough criterion \(W>\frac{1}{3}D\). However, we made no attempt to quantify the axial variation of the surface slope in our drums.

### 3.3 Locating the transition

To locate the slumping-to-rolling transition, we use the diagnostics, \(D_{skew}\) and \(\sigma \). These quantities are collected together for all the sweeps with glass spheres in Figs. 6 and 7.

*d*/

*D*of particle to drum diameter, but only very slightly with drum width. As shown in Fig. 6b, the spread in \(\varOmega _c\) can be largely suppressed by formulating the scaled Froude number,

*W*(see Sect. 3.5).

*i.e.*for increasingly small particles or big drums; for example, for a 1m diameter drum filled with millimeter-size particles, rotation periods of hours would be needed to observe episodic avalanches). Neither transition criterion is completely consistent with estimates given in previous literature [17, 24, 27]. Since the exponents \(\alpha \) and

*a*are not significantly different from unity, the estimates of Liu et al. [24] show the same dependence on drum and particle diameter. These authors, however, also express the transition criteria in terms of the starting and stopping angles \(\theta _{\mathrm {start}}\) and \(\theta _{\mathrm {stop}}\), which they take to be material constants. In fact, these quantities depend on drum and particle geometry, as described in Sect. 3.5 and already documented in the literature (e.g. [6, 14]).

### 3.4 Continuous flow

*C*, is used in the plot for the entire data set. Here, the continuous flow regime is defined as \(D_{skew}<D_{crit}=0.01\), which is slightly smaller than in Fig. 6, but helps to ensure that all the data are above the transition; the choice leads to a minor improvement in fits to the data but is otherwise inconsequential. Only at low rotation rates is there any discernible departure from (4), where the impending transition to episodic avalanching prompts the data to flatten out. Other than this feature, the mean slope data offer little warning of the transition. Indeed, the flattening of the mean slopes is consistent with the noise-driven emergence of incipient episodic avalanching which raises slope angles (see Fig. 2); if one were to delete any such events from the time series of \(\theta (t)\), the mean surface slopes may well continue the linear trend to even lower rotation rate.

*C*, of the fits show some dependence on the drum diameter and width. We quote the values of \(\theta _1\) for \((D,W)=(287,110)\) mm in Table 1. As shown in the lower panels of Fig. 8, much of the dependence on drum width can be suppressed by using additional fits of the form,

*d*/

*D*(Fig. 8c). The adjusted parameters, \(C-\beta _cd/W\), do not vary significantly with

*d*/

*D*; the remaining scatter in Fig. 8d more likely represents differences in surface properties or dispersivity between the different spheres.

### 3.5 Slumping statistics

The wider spread in the starting angle distribution in the narrower drums reflects higher variability in the strength of the spheres due to confinement and, as we show later, is much less prominent for sand. One interpretation of the variability in the bridging effect is that force chains appear for some packings and not others, and more often for spheres than for sand. Moreover, isolated stress-supporting structures of this kind are more likely to inhibit the onset of flow rather than interrupt it, thus not impacting the stopping angle.

*d*/

*D*are included in Fig. 10a, b. The parameters, \(\beta _\mathrm{start,stop}\), are plotted in Fig. 10c and are consistent with the fitting parameters \(\beta _1\) used for the continuous flow data in Fig. 8 (which are also plotted), and values reported previously [6, 14].

*B*); i.e. for a given avalanche, the higher starting angle, the larger the avalanche (cf. Caponeri et al. [4]). As pointed out by Fischer et al. [11], the data also suggest a weak negative correlation between \(\theta _{\mathrm {start}}\) and the subsequent \(\theta _{\mathrm {stop}}\) (data labeled

*A*); the higher the start, the lower the stop. The weakness of this correlation implies that intrinsic noise and dissipation during flow are sufficient to wipe out much of the memory of the initiation of the avalanche.

Despite what is commonly assumed in the literature (e.g. [33]), the plots also suggest a comparable correlation of \(\theta _{\mathrm {start}}\) against the *previous* \(\theta _{\mathrm {stop}}\). Indeed, as shown in Fig. 12, the magnitude of the average correlation of \(\theta _{\mathrm {start}}\) with either the subsequent or previous \(\theta _{\mathrm {stop}}\) is about 0.25 over the episodic range for the narrowest drums (the correlations are again largely independent of \(\varOmega \) in this regime\(^{\circledS 37}\)). The correlations become stronger as the drum is widened, before falling off somewhat for the widest drums, perhaps because of the axial decorrelation of successive avalanches.

A correlation between \(\theta _{\mathrm {start}}\) and the preceding \(\theta _{\mathrm {stop}}\) is possible when the packing of material at the termination of an avalanche, reflecting to some degree the \(\theta _{\mathrm {stop}}\), affects subsequent failure, i.e. \(\theta _{\mathrm {start}}\). However, each avalanche uncovers fresh material in the upper parts of the drum, with a packing set by a much earlier collapse. Nevertheless, for spheres, failure does not always occur first at the top of the slope but can be elsewhere along the surface (Sect. 3.1), where the packing may have been set by the previous avalanche.

### 3.6 Mean avalanche durations and profiles

### 3.7 Spectra

In addition to the main peak, the spectrum of the synthetic signal is flat at low frequency where avalanches look like a random succession of impulses (cf. [4]). For \(\omega _* \ll \omega \ll \langle t_A \rangle ^{-1}\), the solid-body rise of the signal becomes resolved, but not the relatively rapid avalanches, so the signal resembles a sawtooth with the spectrum falling like \(\omega ^{-2}\). Finally, for \(\omega \gg t_A^{-1}\), the continuity of the signal over the avalanches is resolved and the spectrum then falls like \(\omega ^{-4}\). With an avalanche duration of a few seconds (Fig. 13), the cross-over in the tail of the spectrum occurs for \(\omega \sim t_A^{-1}\sim 1\) rad/s, in rough agreement with the switch in scalings of the top curves in Fig. 15.

## 4 Sand

### 4.1 Avalanche phenomenology for sand

### 4.2 Sweeps, intermittency and hysteresis

For both the biggest and smallest drums with \((D,W)=(287,110)\) and (100, 31) mm a smooth transition with clear intermittent switching between phases of slumping and rolling is again evident (see the lower traces in Fig. 17 and the sweep data in Fig. 19b). However, for all the other drums the transition was different, occurring *via* a sudden jump from rolling to slumping or *vice versa*. Moreover, the jump from slumping to rolling occurred at higher rotation rates than the jump from rolling to slumping, leading to hysteresis in the sweep data; see Fig. 19a. Note that multiple sweeps focusing on the transition are included in this figure; these demonstrate how the transitions between the two states do not occur at a single rotation rate but at seemingly random values of \(\varOmega \) spread over ranges that are narrower than the window of hysteresis.

It is also not clear why the window of hysteresis opens in between our largest and smallest drums. Conceivably, enhanced fluctuations with fewer particles might wash out a hysteretic transition in the smallest drum; perhaps the opportunity for spatial decorrelation triggers additional perturbations to rationalize why the biggest drum shows an intermittent transition. Either way, the window of hysteresis likely closes at the two extremes due to an increase in the effective system noise.

### 4.3 Avalanche statistics and profiles for sand

Figure 22 shows slumping statistics for sand; the corresponding starting-stopping-angle correlations are compared with results for glass spheres earlier in Fig. 12. Figure 22 illustrates how the dependence of the starting angle distribution on drum width is much less marked for sand. Moreover, in the wider drums, the starting and stopping angles remain well separated, furnishing a more Gaussian-like amplitude distribution that favors regular avalanching rather than collapses of arbitrarily low amplitude. The sand amplitude distribution is consequently sensitive to drum diameter but has no clear dependence on width\(^{\circledS 38,39}\), unlike that for spheres.

The correlations between the starting and stopping angles are also different for sand (Fig. 12b). In the narrow drums, \(\theta _{\mathrm {start}}\) is poorly correlated with the previous \(\theta _{\mathrm {stop}}\), consistent with the observation that the avalanches begin at the top of the drum, where fresh material has been exposed by the previous avalanche and the packing is relic from the distant past. The starting angle, however, is strongly negatively correlated with the subsequent stopping angle, and so dissipation and dynamical noise during flow cannot erase the memory of avalanche initiation. Widening the drum strengthens the correlation of \(\theta _{\mathrm {start}}\) with the preceding \(\theta _{\mathrm {stop}}\) whilst reducing its correlation with the subsequent \(\theta _{\mathrm {stop}}\). In the widest drums, \(\theta _{\mathrm {start}}\) is roughly equally correlated with both (coefficients of about \(\pm \,0.5\)). Evidently, the wider drum features greater dynamical noise that suppresses the memory of initiation; the correlation with the previous start is less straightforward to understand.

Sample avalanche profiles for sand are shown in Fig. 23. Once again \(t_A\) increases logarithmically with rotation period due to the increasing time taken to initiate and terminate each avalanche. For wider drums, the time needed to start the avalanche dominates, whereas the time taken to end the event is more critical in narrower drums. The avalanche profiles contain more structure than their relatives for spheres (cf. Fig. 14). Most noticeable is the kink near the midpoint of the profile, which is caused by the two fronts that switch flow on and off: the kink occurs when the advancing front that mobilizes flow reaches the bottom of the sand surface and reflects into the retreating front that arrests motion.

The preceding observations suggest a physical picture of sand avalanche dynamics: in the wider drums, the two fronts fully traverse the granular surface. The triggering front takes time to start at the lower rotation rates, increasing the avalanche time and reducing the memory on the starting angle. When the arresting front returns to the top of the drum to switch off the avalanche, it partially sets the packing there, dictating when the next avalanche begins and correlating \(\theta _{\mathrm {stop}}\) with the following \(\theta _{\mathrm {start}}\). In the narrower drums, sidewall friction slows and weakens the arresting front so that the avalanche takes longer to terminate and the packing at the top of the drum is set by an earlier collapse, decorrelating \(\theta _{\mathrm {stop}}\) and the next \(\theta _{\mathrm {start}}\).

### 4.4 Sand spectra

Figure 25 illustrates the clear switch in the dominant spectral peak when the transition is hysteretic (compare the blue and red points). For the continuous flow data plotted in this figure sloshing modes have yet to appear and the spectral peak characterizes noisy flow fluctuations. The resulting characteristic frequency is clearly distinct from that for episodic avalanching, which once more reflects the typical avalanche spacing (fits of the form (8) again furnish a fair representation of the data; see Fig. 25). Evidently, the transition arises when the slumping and rolling frequencies are well matched, much as suggested previously in some qualitative prescriptions (e.g. [17, 27]).

## 5 Conclusions

In this paper we have reported an experimental survey of episodic avalanching and continuous flow in a granular drum. This device is a classical arrangement to study granular dynamics, yet a detailed investigation of the two regimes and the transition between them has not previously been presented. We considered a variety of different granular media (glass spheres with a range of diameters and a sand) and drums with different diameters and widths. Our main advance was to catalog the dynamics over lengthy sweeps in rotation rate, afforded by an efficient data acquisition system. Sweeps could be conducted for days or even weeks, allowing us to collect relatively clean statistics of episodic avalanching or the vagaries of continuous flow. From the experiments we have characterized the properties of the two regimes and the intervening transition, which sets the stage for modeling efforts to match the observations and test theories.

For most of our spheres and drums, the transition from episodic avalanching to continuous flow takes the form of a gradual switch in dynamical behavior wherein the two phases are blended in varying degrees. As the particle radius becomes small, the blend becomes refined into an alternation between clearly defined phases of continuous flow or episodic avalanching (cf. [12]). For sand, the transition is again intermittent in either the biggest or smallest drums, but in all others a hysteretic transition takes place [32]. Overall, the different forms of the transition are suggestive of a system in which there are two possible states and which is perturbed by differing degrees of noise. The transition is a smooth blend in behavior for higher noise levels, hysteretic for weak noise, and intermittent in between. There is little sign that the continuous flow state disappears in some kind of a deterministic bifurcation at low rotation rates, or that episodic avalanching terminates at higher rotation rates in another bifurcation. In other words, the transition explored here is noisier, but follows the general scenario outlined in [12].

The results for glass spheres suggest that the transition is largely independent of drum width and arises roughly for \(0.3< \mathrm {Fr}(D/d) < 0.5\), in terms of the Froude number, \(\mathrm {Fr}=\varOmega \sqrt{D/g}\). This criterion is consistent with previously reported results for spheres [3, 12], but does not work for sand which displays a more complicated dependence on the drum geometry. The criterion is different to a number of existing predictors of transition based mostly on heuristic arguments, although it is similar to one proposed by Liu et al. [24] for angular particles such as sand, but not glass spheres. In any event it is hard to see how to reconcile the heuristic arguments underlying these other predictors with the nature of the transition as they take no explicit account of effect of dynamical noise. We also find little support for a suggestion [19] that the transition is connected to the flow-depth-surface-angle relation for sheet flow to cease on an inclined plane (see Appendix B).

Although we have resisted providing any detailed theoretical models to complement our experiments, these are certainly possible. Indeed, we conducted simulations with the Discrete Element Method in tandem with the experiments, and which helped guide some of our scalings and fits of the data. A brief discussion of a model for a relatively narrow drum based on the *mu*(*I*) law is provided in Appendix B. One can also build cruder ODE models (e.g. [4]). To capture the experimental observations, stochastic forcing is essential in these models. Moreover, two types of noise are needed: fluctuations in packing are required to furnish a random starting angle for an avalanche, and dynamical noise during flow is needed to recover a random stopping angle. With both types of noise suitably incorporated, models can be designed that show some qualitative agreement with the observations. However, many of the finer details (such as the distributions and correlations of the starting and stopping angles) are likely to be awry without additional empirical input.

A persistent ageing effect plagued our efforts to generate reproducible results. We eliminated this feature by suitably maturing particles in high-speed burn-in experiments, and by restricting our use of glass spheres with smaller diameters. Polydispersivity may constitute another intrinsic problem, with segregation potentially also leading to long-time evolution. Overall, the surface angle during both episodic avalanching or continuous flow is sensitive to ageing effects and drum or particle geometry, and is likely to be significantly affected by external noise in less controlled situations. One should exercise caution in using such a statistic to characterize granular dynamics (cf. [21]); other, more robust measures offer greater diagnostic value.

Beyond the rotating drum, one may wonder what kinds of intermittent motions occur in other flow configurations. Episodic avalanches also arise in heap flows and sandpiles fed at low flux (e.g. [2, 19, 22]), and similar intermittent motions occur underneath plates dragged over granular layers [28]. In sheet flow down an incline (e.g. [13]) or for bulldozed sandpiles [35], however, episodic avalanching does not occur at low flow rates. For the inclined plane, fluctuations during continuous flow trigger the arrest of flow, but once grains stop noise cannot drive the system back into motion, precluding any recurring slumping state. For the bulldozer, there is again a continuous flow state, but the driving appears to preclude any locked-up arrangement like rigid rotation. Stochastic fluctuations can then only agitate the system about the continuous flow state.

## Notes

### Acknowledgements

We thank Greg Wagner and Quentin Debray for assistance and discussions.

### Compliance with ethical standards

### Conflict of interest

The authors declare no conflict of interest.

## Supplementary material

## References

- 1.Bocquet, L., Charlaix, E., Ciliberto, S., Crassous, J.: Moisture-induced ageing in granular media and the kinetics of capillary condensation. Nature
**396**(6713), 735–737 (1998)ADSCrossRefGoogle Scholar - 2.Börzsönyi, T., Halsey, T., Ecke, R.: Avalanche dynamics on a rough inclined plane. Phys. Rev. E
**78**(1), 011306 (2008)ADSCrossRefGoogle Scholar - 3.Brucks, A., Arndt, T., Ottino, J., Lueptow, R.: Behavior of flowing granular materials under variable g. Phys. Rev. E
**75**(3), 032301 (2007)ADSCrossRefGoogle Scholar - 4.Caponeri, M., Douady, S., Fauve, S., Laroche, C.: Dynamics of avalanches in a rotating cylinder. In: Guazzelli, E., Oger, L. (eds.) Mobile Particulate Systems, pp. 331–366. Springer, Dordrecht (1995)CrossRefGoogle Scholar
- 5.Courrech du Pont, S., Gondret, P., Perrin, B., Rabaud, M.: Granular avalanches in fluids. Phys. Rev. Lett.
**90**(4), 044301 (2003)ADSCrossRefGoogle Scholar - 6.Courrech du Pont, S., Gondret, P., Perrin, B., Rabaud, M.: Wall effects on granular heap stability. EPL (Europhys. Lett.)
**61**(4), 492 (2003)ADSCrossRefGoogle Scholar - 7.Davidson, J., Scott, D., Bird, P., Herbert, O., Powell, A., Ramsay, H.: Granular motion in a rotary kiln: the transition from avalanching to rolling. KONA Powder Part. J.
**18**, 149–156 (2000)CrossRefGoogle Scholar - 8.Ding, Y., Forster, R., Seville, J., Parker, D.: Granular motion in rotating drums: bed turnover time and slumping–rolling transition. Powder Technol.
**124**(1), 18–27 (2002)CrossRefGoogle Scholar - 9.Dury, C., Ristow, G., Moss, J., Nakagawa, M.: Boundary effects on the angle of repose in rotating cylinders. Phys. Rev. E
**57**(4), 4491 (1998)ADSCrossRefGoogle Scholar - 10.Félix, G., Falk, V., D’Ortona, U.: Granular flows in a rotating drum: the scaling law between velocity and thickness of the flow. Eur. Phys. J. E Soft Matter Biol. Phys.
**22**(1), 25–31 (2007)CrossRefGoogle Scholar - 11.Fischer, R., Gondret, P., Perrin, B., Rabaud, M.: Dynamics of dry granular avalanches. Phys. Rev. E
**78**(2), 021302 (2008)ADSCrossRefGoogle Scholar - 12.Fischer, R., Gondret, P., Rabaud, M.: Transition by intermittency in granular matter: from discontinuous avalanches to continuous flow. Phys. Rev. Lett.
**103**(12), 128002 (2009)ADSCrossRefGoogle Scholar - 13.Forterre, Y., Pouliquen, O.: Flows of dense granular media. Annu. Rev. Fluid Mech.
**40**, 1–24 (2008)ADSMathSciNetCrossRefMATHGoogle Scholar - 14.MiDi, G.D.R.: On dense granular flows. Eur. Phys. J. E
**14**, 341–365 (2004)CrossRefGoogle Scholar - 15.Gray, J.M.N.T.: Granular flow in partially filled slowly rotating drums. J. Fluid Mech.
**441**, 1–29 (2001)ADSMathSciNetCrossRefMATHGoogle Scholar - 16.Henein, H., Brimacombe, J., Watkinson, A.: Experimental study of transverse bed motion in rotary kilns. Metall. Trans. B
**14**(2), 191–205 (1983)CrossRefGoogle Scholar - 17.Henein, H., Brimacombe, J., Watkinson, A.: Modelling of transverse solids motion in rotary kilns. Metall. Trans. B
**14**(2), 207–220 (1983)CrossRefGoogle Scholar - 18.Jenkins, J.T., Berzi, D.: Dense inclined flows of inelastic spheres: tests of an extension of kinetic theory. Granul. Matter
**12**(2), 151–158 (2010)CrossRefMATHGoogle Scholar - 19.Jop, P., Forterre, Y., Pouliquen, O.: Crucial role of sidewalls in granular surface flows: consequences for the rheology. J. Fluid Mech.
**541**, 167–192 (2005)ADSCrossRefMATHGoogle Scholar - 20.Khakhar, D., McCarthy, J., Ottino, J.: Radial segregation of granular mixtures in rotating cylinders. Phys. Fluids
**9**(12), 3600–3614 (1997)ADSCrossRefGoogle Scholar - 21.Kleinhans, M., Markies, H., De Vet, S., Postema, F., et al.: Static and dynamic angles of repose in loose granular materials under reduced gravity. J. Geophys. Res. Planets
**116**(E11), 1–13 (2011)CrossRefGoogle Scholar - 22.Lemieux, P.A., Durian, D.: From avalanches to fluid flow: a continuous picture of grain dynamics down a heap. Phys. Rev. Lett.
**85**(20), 4273 (2000)ADSCrossRefGoogle Scholar - 23.Lim, S.Y., Davidson, J., Forster, R., Parker, D., Scott, D., Seville, J.: Avalanching of granular material in a horizontal slowly rotating cylinder: Pept studies. Powder Technol.
**138**(1), 25–30 (2003)CrossRefGoogle Scholar - 24.Liu, X., Specht, E., Mellmann, J.: Slumping–rolling transition of granular solids in rotary kilns. Chem. Eng. Sci.
**60**(13), 3629–3636 (2005)CrossRefGoogle Scholar - 25.Lumay, G., Vandewalle, N.: Flow of magnetized grains in a rotating drum. Phys. Rev. E
**82**(4), 040301 (2010)ADSCrossRefGoogle Scholar - 26.Maneval, J., Hill, K., Smith, B., Caprihan, A., Fukushima, E.: Effects of end wall friction in rotating cylinder granular flow experiments. Granul. Matter
**7**(4), 199–202 (2005)CrossRefGoogle Scholar - 27.Mellmann, J.: The transverse motion of solids in rotating cylinders-forms of motion and transition behavior. Powder Technol.
**118**(3), 251–270 (2001)CrossRefGoogle Scholar - 28.Nasuno, S., Kudrolli, A., Bak, A., Gollub, J.P.: Time-resolved studies of stick-slip friction in sheared granular layers. Phys. Rev. E
**58**(2), 2161 (1998)ADSCrossRefGoogle Scholar - 29.Orpe, A., Khakhar, D.: Scaling relations for granular flow in quasi-two-dimensional rotating cylinders. Phys. Rev. E
**64**(3), 031302 (2001)ADSCrossRefGoogle Scholar - 30.Orpe, A., Khakhar, D.: Rheology of surface granular flows. J. Fluid Mech.
**571**, 1–32 (2007)ADSMathSciNetCrossRefMATHGoogle Scholar - 31.Pouliquen, O., Forterre, Y.: Friction law for dense granular flows: application to the motion of a mass down a rough inclined plane. J. Fluid Mech.
**453**, 133–151 (2002)ADSCrossRefMATHGoogle Scholar - 32.Rajchenbach, J.: Flow in powders: from discrete avalanches to continuous regime. Phys. Rev. Lett.
**65**(18), 2221 (1990)ADSCrossRefGoogle Scholar - 33.Rajchenbach, J.: Granular flows. Adv. Phys.
**49**(2), 229–256 (2000)ADSCrossRefGoogle Scholar - 34.Rajchenbach, J.: Dynamics of grain avalanches. Phys. Rev. Lett.
**88**(1), 014301 (2002)ADSCrossRefGoogle Scholar - 35.Sauret, A., Balmforth, N., Caulfield, C., McElwaine, J.: Bulldozing of granular material. J. Fluid Mech.
**748**, 143–174 (2014)ADSCrossRefGoogle Scholar - 36.Tegzes, P., Vicsek, T., Schiffer, P.: Development of correlations in the dynamics of wet granular avalanches. Phys. Rev. E
**67**(5), 051303 (2003)ADSCrossRefGoogle Scholar

## Copyright information

**Open Access**This article is distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution, and reproduction in any medium, provided you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons license, and indicate if changes were made.