Ram Sudhir
Sharma
a and
Alban
Sauret
*bc
aDepartment of Mechanical Engineering, University of California, Santa Barbara, California 93106, USA. E-mail: ramsharma@ucsb.edu
bDepartment of Mechanical Engineering, University of Maryland, College Park, Maryland 20742, USA. E-mail: asauret@umd.edu
cDepartment of Chemical & Biomolecular Engineering, University of Maryland, College Park, MD 20742, USA
First published on 3rd February 2025
Granular materials are involved in most industrial and environmental processes, as well as many civil engineering applications. Although significant advances have been made in understanding the statics and dynamics of cohesionless grains over the past decades, most granular systems we encounter often display some adhesive forces between grains. The presence of cohesion has effects at distances substantially larger than the closest neighbors and consequently can greatly modify their overall behavior. While considerable progress has been made in understanding and describing cohesive granular systems through idealized numerical simulations, controlled experiments corroborating and expanding the wide range of behavior remain challenging to perform. In recent years, various experimental approaches have been developed to control inter-particle adhesion that now pave the way to further our understanding of cohesive granular flows. This article reviews different approaches for making particles sticky, controlling their relative stickiness, and thereby studying their granular and bulk mechanics. Some recent experimental studies relying on model cohesive grains are synthesized, and opportunities and perspectives in this field are discussed.
Natural contact adhesion between grains can come from various physical sources, such as solid bonds,5–7 van der Waals forces and electrostatic forces,8,9 small capillary bridges formed by the condensation of vapor or the addition of liquid.10–13 Despite mainly limiting such interactions to immediate neighbors, inter-particle cohesive forces can considerably change the force fabric within the granular assembly and, consequently, its bulk mechanics.14 Recent experiments with model contact adhesion between model particles such as glass beads are being used to study granular mechanics from the scale of particles to the scale of bulk processes in a controlled manner. Probing how the magnitude of adhesion, among other particle scale properties, affects bulk behavior of cohesive assemblies remains a major experimental challenge as model approaches for controlled inter-particle adhesive forces are still being developed. In this manuscript, we review the progress in our study of cohesive granular materials through controlled experiments, with a particular emphasis on different model cohesive grains that have been used to conduct experiments in the literature.
Research to improve our current understanding and modeling of the macroscopic behavior of granular materials comes from the need and desire to control bulk powders and grains for storage and use as described by particle technology,15,16 or through our understanding of soil6,17 and other natural materials.2,18,19 In natural granular materials, the distribution of particle properties is often very large, resulting in simplified, statistical descriptions.20 The simplifications required to overlay testable properties onto non-idealized granular materials, such as most industrial powders, are often so severe that tested properties are only used to characterize grains. Characterization refers here to the use of empirical tests to differentiate between grain species rather than describe their behavior on the basis of clear physical principles. This last point is precisely the large success of the progress made over the last few decades in describing the static and dynamic properties of model cohesionless granular materials.21 The discovery of critical parameters in describing the bulk dynamics of granular assemblies resulted in the development of statistical descriptions of bulk flows through some model rheologies.22–24 However, results obtained for non-cohesive grains are usually not applicable when a adhesion comes into play, for instance, to account for resistance to deformation due to cohesion. Altogether, this highlights a need for good experimental models of cohesive grains, where the properties of such systems can be studied across length, time, and stress scales.
Most fundamental studies devoted to cohesive granular materials consider capillary cohesion induced by the presence of liquid owing to its relative experimental simplicity.12,13 The addition of a small amount of water, as shown in Fig. 1 may be familiar from building sandcastles, can dramatically change the mechanics of a granular material. When wet granular materials are sheared or flow, liquid bridges break and merge, generating localized and heterogeneous effects, making the development of a general framework quite challenging. Reviews specifically on wet grains have been written by Herminghaus13 and Mitarai and Nori,12 for instance. In the case of powders, which are grains of diameter a few tens of microns and smaller, cohesion may also be a consequence of other forces such as van der Waals or some charging. Delineating the precise cause of adhesion in most cases is not straightforward,25 so an important goal is to be able to describe the effects of cohesion at a scale where the physical source of stickiness is not particularly relevant. Altogether, there is a strong need to develop our understanding of the physics of cohesive grains and their collective behavior using a range of physical sources. Being able to experimentally engineer and control the adhesion between particles would pave the way to significant advancements in our understanding of cohesive granular mechanics, such as flow, stability, and erosion.
Cohesion in powders arising from van der Waals forces is often described from generalizing theoretical derivations, e.g., Derjaguin–Muller–Toporov (DMT)26 or some model experiments developed on Johnson–Kendall–Roberts (JKR),27 describing adhesive contact mechanics between particles based on particle stiffness.28 Such contact descriptions can be used to develop general numerical models for cohesive powders. Such models have also been used to describe how a rheological description of granular flow is modified due to cohesion.3 The goal of this review is not to cover such models or their consequences but instead to focus on experimental approaches to model and understand cohesion. Such experimental approaches are a step closer to complex assemblies of cohesive particles observed in nature or in industrial processes.
For the sake of consistency, we use adhesion to refer to individual stickiness between two grains or between a grain and another surface. We use cohesion, similar to fluids, to refer to the general stickiness amongst an assembly of particles. Consequently, for describing individual bonds and sources, we use the phrase adhesion, while our primary interest lies in reviewing experiments probing the mechanics of cohesive assemblies of grains. Another linguistic difference is often drawn between the definitions of powders and grains. Usually, such a distinction is made based on particle size, with particles smaller than 100 μm separately called powders. At the scales of powders, cohesion is usually un-ignorable: van der Waals’ forces are usually comparable to the particle weight (as shown in Fig. 2(a)) or as mentioned earlier, humidity and electrical charging can cause such particles to be sticky. For this article, we are interested in the cases where cohesion can be intentionally introduced, so drawing such a distinction between powders and other grains is not particularly helpful here. We do, however, omit discussions of colloids, i.e. particles that are small enough to be motivated by thermal fluctuations.
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| Fig. 2 (a) Comparison of the order of magnitude of the particle weight, the air drag force, and different interparticle forces when varying the size of a spherical particle of roughness 50 nm. The expressions used to make this schematic, alongside the magnitudes and descriptions of the constants, are summarized in Table 1. (b) Schematic illustration of micromechanical tests of adhesion between particles in a normal and shear configuration. Pictures of such experiments are shown in (c) and (d), respectively. (c) and (d) are reproduced from Hemmerle et al.29 with permission from the Royal Society of Chemistry. | ||
This review is divided into two main parts. In the first part, we review different techniques to induce cohesion in a controlled manner, with attention paid to the advantages and drawbacks of each. In the second part, the observed effects of cohesion in experiments are summarized, both at the particle scale and at macroscopic scales. A comprehensive review of bulk mechanics with the relevant derivations can be found in most textbooks on the subject, e.g., ref. 30–35, with only the relevant characterization discussed here. Following characterization, we briefly summarize the different experimental geometries & configurations used with model cohesive grains for each scale. Attempts to bridge these two characterizations are discussed. Finally, some perspectives are provided on avenues of future research.
| Sources of adhesion | Expressions for Fadh in Fig. 2(a) | Model system | Const. | Description | Value |
|---|---|---|---|---|---|
| Capillary bridges |
F
adh = πγd cos θ |
Liquid, glass spheres12 | γ | Surface tension | 72 mN m−1 |
| θ | Wetting angle | 0° | |||
| Solid bridges | F adh = kπσgpξp1/2(d/2)2 | Solid binder, glass spheres39 | k | Numerical prefactor | 1.62 |
| σ gp | Adhesive strength | 275 mN m−1 | |||
| ξ p | Relative volume | 0.005 | |||
| Polymer coatings | F adh = kπγPDMSd(1 − e−b/B) | Cross-linked PDMS-OH/H3BO3, glass spheres40 | k | Numerical prefactor | 1.5 |
| γ PDMS | Surface tension | 24 mN m−1 | |||
| b | Coating thickness | 1 mm | |||
| B | Roughness related | 230 nm | |||
| van der Waals | F adh = AH(d/2)/(12ε2) | Attraction between two spheres28 | A H | Hamaker constant | 6.5 × 10−20 |
| ε | Surface roughness | 50 nm | |||
| Other relevant forces | Expressions for F in Fig. 2(a) | Model system | Const. | Description | Value |
|---|---|---|---|---|---|
| Particle weight | F w = kρggπd3 | Glass sphere | k | Numerical prefactor | 1/6 |
| ρ g | Density of glass | 2500 kg m−3 | |||
| g | Gravitational acc. | 9.8 m s−2 | |||
| Air drag | F drag = kCdρaUa2A | Drag on a sphere due to air37 | k | Numerical prefactor | 1/2 |
| A = π(d/2)2 | C d | Drag coefficient | Col 2. | ||
| C d = 2.7 + 21.7/Re + 0.1/Re2 + 12.2/Re0.2 − 10.6/Re0.1 | ρ a | Density of air | 1.2 kg m−3 | ||
| U a | Velocity of air | 0.5 m s−1 | |||
| Re | Reynolds’ num. | U a d/νa | |||
| ν a | Dyn. viscosity of air | 1.6 × 10−5 Pa s | |||
Experimentally, direct measurements are required to measure the adhesive force when separating two grains until the rupture of the bond [Fig. 2(b)]. Usually, the maximum tension force measured during the entire test and before splitting is considered as the representative adhesive force Fadh. Although the most common approach is to measure the tension force when the particles are separated along their axis [Fig. 2(c)], other yielding limits such as shear [Fig. 2(d)] or torsion can also provide information on the cohesive force and the breaking of the bond.29,39 The inter-particle adhesive forces lead to macroscopic cohesion, which depends on the amplitude of the force, as well as the number of particles that are in contact with each other, the packing fraction, or the friction coefficient. At the macroscopic scale, one can introduce τc = μσt, the cohesive yield stress of the material. For a stress applied larger than τc, the cohesive granular material starts deforming plastically. Inside the macroscopic structure, when this happens, the adhesive force between some particles breaks and allows the material to rearrange. The notion of cohesion at the macroscopic scale and the relation with the inter-particle cohesion will be discussed in more detail in Section 4.
When using wet grains as a model material, one must consider different factors. Various interstitial fluids have been used in experiments, but the choice of the fluid can significantly influence the dynamics of the granular media. The most common fluid used is water due to the simplicity of preparing the material, handling it, and then drying it to retrieve a dry granular material. Glycerol, or mixtures of water and glycerol, is another interstitial fluid frequently utilized in experiments. The mixture allows studying the influence of fluid viscosity on the dynamics of the wet, cohesive granular material. One issue when using water, or mixtures with water, is that one must be careful with evaporation as the fraction of water in the macroscopic granular material will evolve over time. In addition, the evaporation of the liquid can bring some heterogeneities in the material as the evaporation starts from the free surface of the granular material. As a result, silicone oil and mineral oils are also used, in part to avoid evaporation but also due to their controlled rheological properties.
To prepare a wet granular material with controlled cohesion, achieving a homogeneously mixed granular material is essential. A possible method involves using a stand mixer, where the grains and the liquid are initially poured with the desired proportion and then mixed thoroughly for a sufficiently long time. The total amount of humidity is often described by the volume or mass ratios of the solid and liquid phases. For Fig. 1 and 3, a mass ratio W = mliq/mliq+solid, where mliq and msol are the total masses of the liquid and solid phases mixed respectively. One potential issue when using water or volatile liquids is that they can evaporate and alter the macroscopic cohesion. For situations where evaporation is a concern, grains, and liquid can be mixed within a sealed, rotating drum or a tube placed on a roller mixer. In this case, weighing the container before and after mixing can help verify the amount of liquid adhering to the wall of the container to make sure to start with the desired value of W.
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| Fig. 3 Schematic representation of the distribution of liquid within a wet granular material as a function of the liquid fraction W and corresponding examples: (a) dry grains; (b) pendular state [reproduced with permission from Herminghaus.13 Copyright 2005 from Taylor & Francis]; (c) funicular state; (d) capillary state [reproduced from Sauret et al.43]. If the liquid fills all the pore spaces and makes a suspension, the effects of cohesion are no longer observed, and this state is consequently outside our interest here. (e) Evolution of the capillary force with the distance between the particles and different volumes of capillary bridges [adapted with permission from Willett et al.44 Copyright 2000 American Chemical Society]. While more liquid ensures a bridge can last for a greater separation length, the maximum force appears to be approximately the same. (f) Cohesive yield stress τc measured with a shear cell when varying the liquid fraction W [reprinted with permission from Richefeu et al.45 Copyright 2006 by the American Physical Society]. The dashed line is drawn to suggest that beyond some minimal amount of liquid content, Wm, the yield stress is observed to saturate to cm, for the ratio of liquid to total mass tested here. | ||
At the microscopic scale, the capillary bridge force depends on the physical properties of the particles (size and shape, wettability, roughness, etc.), the fluid properties (surface tension, viscosity, volume, etc.) as well as the ambient conditions (pressure, temperature).11,46 The adhesive force due to a capillary bridge of two spherical grains of radius R in contact and connected by a capillary bridge is:
Fadh = 2πγR cos θ, | (1) |
Eqn (1) provides the amplitude of the inter-particle adhesion and can be used to estimate the bond number at the particle scale. In a static or flowing granular material, not all capillary bridges have the same volume and are between particles in contact, and some particles move relatively to each other. At the particle scale, different studies have generalized eqn (1) to the case of spheres separated by a distance of D, showing, in this case, a weak dependence on the volume of the capillary bridge, as illustrated in Fig. 3(e).47–49 The relative motion of the grains leads to the deformation of capillary bridges, which in turn induces viscous forces that resist the movement of particles within it. Different models have been developed at the particle scale to account for the fluid viscosity, particle size, separation velocity, and the dimensionless distance between the grains.50
We should also emphasize that, contrary to various numerical models, an important characteristic of the cohesion introduced by liquid bridges is its hysteretic nature. Indeed, a capillary bridge forms between two grains when the liquid films covering them come into contact and coalesce. This occurs at very short distances, on the order of surface roughness. However, the presence of the capillary bridge, and thus some force, is maintained until it breaks, which only happens at distances comparable to the size of the grains. Various parameters govern this distance, and in particular, the volume of the liquid bridge.48,51,52 The viscosity of the liquid and the separation velocity can also impact this rupture length.49,53 In addition, for a given volume of the capillary bridge, the contact angle of the liquid wetting the particle can exhibit some pinning during the relative motion of the particles and thus some variation of the capillary force.54,55
Capillary interactions have been characterized at the scale of two grains for Newtonian fluids, but taking them into account in a granular packing is more challenging. The heterogeneous spatial distribution of the liquid locally modifies the mechanical properties of the wet granular material. The different states of a wet granular material are, in ascending order of liquid fraction, the dry state (without liquid), pendular state, funicular state, and capillary state, as illustrated in Fig. 3(a)–(d).12,13 The pendular regime occurs at low liquid contents, typically below 5% by mass for monodisperse glass beads. It is characterized by the formation of isolated liquid bridges between particles rather than a continuous liquid phase. The network of liquid bonds induces capillary attraction, leading to a macroscopic cohesion τc.56 The funicular state occurs at water fractions (per mass) ranging from approximately 5% to 20%. Within this range, the liquid content is sufficient to enhance cohesion through the formation of liquid bridges while still allowing for the coexistence of both liquid-filled pores and dry pores within the material. The capillary state for an assembly of glass beads typically lies between approximately 20% and 40% of liquid by mass.57 Beyond this, a suspension is obtained, and no more cohesion is observed.58
Different studies have considered the macroscopic shear strength properties of wet granular materials in the pendular state. In particular, Richefeu et al.45 have investigated how water content affects the shear strength of wet granular materials in the pendular state through a combined experimental and numerical approach. They have shown that shear strength primarily depends on the distribution of liquid bonds, resulting in a saturation effect as water content increases and provided an expression for the cohesive stress, similar to the one first proposed by Rumpf:
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The choice of the liquid and the granular material controls the overall cohesion. However, one could also introduce different levels of cohesion between different populations of beads. For instance, Li and McCarthy have used binary mixtures of spherical particles where some particles are more hydrophobic than others, leading to variations in inter-particle cohesion.59,60 Using this system allowed them to study the interplay between cohesive forces and particle size distributions in determining the mixing and segregation behavior of cohesive granular materials.
Finally, although an additional phase is present, we should mention the possibility of making immersed granular materials with controlled inter-particle cohesion. Indeed, one can make capillary suspensions, which consist of particles dispersed in a first liquid phase with a small amount of a secondary liquid that is immiscible with the continuous phase. The secondary liquid creates the capillary bridges between the grains, leading to cohesive effects.61–63
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| Fig. 4 (a) Experiments showing microbial-induced calcite precipitation (MICP) to cement grains for tension tests as described earlier [reprinted with permission from Kwon et al.64]. (b) and (c) Typical set of measurements from particle-scale tensile tests. (b) Evolution of the force between two grains connected by a solid bond. As the distance between rigidly connected spheres increases, the force measured rises until the bond ruptures. The amplitude of the force between before and after the rupture gives the adhesive force. (c) 3D tomographic reconstructions of broken bonds of paraffin wax between 7 mm glass beads. Rupture often occurs as de-bonding from one of the grains (top and middle) or as fracture within the bond (bottom). Fig. (b) and (c) are reproduced with permission from Farhat et al.,39 copyright 2024 Springer Nature. | ||
Even within laboratory-made cemented materials, a wide variety of materials have been used to make solid bonds between glass beads or more angular materials, such as sands. Some of the materials that have been used include salt,65 paraffin,39,66 epoxy,67 polyurethane,68 cement,69 resin,63 or cross-linked PDMS.70 Ideally, the amount of cemented materials introduced must remain small, of the order of 1–5% per weight, so that most of the solid bonds are connected to two particles only. One of the main advantages of this approach is that the cohesion does not usually depend on environmental conditions, such as humidity. However, in some cases, the temperature may be a strong parameter.
To prepare a model cohesive granular material with solid bonds, a binding matrix needs to be added to the particles (sand or glass beads). Different approaches can be used to mix the binder and the grains depending on what material is desired to constitute the solid bonds. The most common one is to introduce the liquid binder to the granular material and mix thoroughly to achieve an even distribution. The mixing can be done similarly to the situation with capillary bridges. This mixture of particles and binder is then poured into a container to form the desired shape for further experiments. Then, the liquid binder (cement, clay, PMDS, epoxy resin, etc.) that is initially forming capillary bridging between the particles is left to dry or react such that it hardens after blending. Another approach that can be used is to induce crystallized solid precipitation, often microbial calcite, directly within the granular structure. This matrix can ultimately exhibit varied spatial distributions, from a nearly uniform grain surface coating to highly localized cementing at grain contacts.
Similar to capillary bridges, the characterization of the cohesion force induced by the solid bond can be done between two particles (Fig. 4(b)). The tensile force required to separate two spheres connected by a solid bond corresponds to the onset of adhesive rupture. Therefore, the amplitude of the force will depend on the properties of the material connecting the particles and the adhesive properties on the surface that depend on the particle (e.g., roughness) and the bonding material. In particular, the rupture of the bond can occur through the detachment of the surface between the solid material and the particle, through the internal failure of the bond, or through a mixed-type bond rupture with some fracture at the bond (Fig. 4(c)).
Recent experiments have shown that for a paraffin bridge between two millimeter-sized spheres, the tensile force Fadh to break the bond can be estimated as39
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The cohesion induced by solid bridges is brittle, so the cohesion vanishes upon the breaking of the bond and is not reformed even when particles are in contact again. This approach has been used to study the initial failure of cohesive granular materials. However, similar brittle cohesion has also been used in DEM simulation for a geophysical context to study the collapse of cohesive cliffs.71
Adjusting the size of the grains or the amount of binder put in the initial system can lead to some control over the relative influence of the cohesion. One can also change the nature of the binder to tune the Young's modulus. Nevertheless, a binding material that does not exhibit a reduction in volume during drying is preferable to avoid pre-stresses and fractures in the cohesive granular material. In addition, depending on the nature of the binder, the solid bridge may not be straightforwardly brittle and may exhibit more exotic mechanics.72–75 It is therefore preferable to use paraffin wax or other relatively simple materials to create model binders.
Similar to the previous discussions, different efforts have been made to correlate the microscopic properties of the solid bonds between two particles to the macroscopic mechanical strength. An approach to studying the macroscopic properties of such materials is to perform compression tests and characterize the failure, e.g. ref. 69, 76 and 77. Another one consists of measuring the force required to separate two inverted cones containing the cohesive material. Overall, the results obtained suggest a relationship between the microscopic and the macroscopic solid bond strength, but more investigations on this point remain to be done to obtain a full picture under different loading conditions. From an analytical perspective, the transition from microscopic to macroscopic behavior in a granular material with solid bonds is achieved using homogenization laws, similar to the work developed by Rumpf.
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| Fig. 5 SEM images of glass beads (a) before and (b) after polymer coating [reprinted from Ma et al.,79 Copyright 2019, with permission from Elsevier]. (c) Macroscopic cohesive stress τc of CCGM measured from inclined plane experiments as a function of the interparticle cohesive force Fc. The dashed line is eqn (2) with ϕ = 0.6 and Z = 6, which seemingly provides a reasonable prediction for polymer-coated grains as well. The inset shows that for the range of coatings tested here, no major effect on macroscopic friction μ is observed. [Reproduced from Gans et al.,40 Copyright 2020, with permission from American Physical Society.] | ||
These cohesive granular materials have mainly been used to study the role of interparticle forces on the fluidization characteristics of particles in gas–solid fluidized beds79,80 or the flow dynamics in a spheronizer.81 Indeed, one advantage of a polymer coating approach is that once a bond between two particles is broken, it can be restored upon further contact, similar to a capillary bridge. Furthermore, there is no transfer of liquid involved or drainage of the capillary bridge by air flows, which could be detrimental to the long-term evolution of the system.
More recently, another approach relying on a polymer coating has been developed by Gans et al., leading to the development of the so-called Cohesion-controlled granular materials (CCGM).40 The production of CCGM typically involves coating borosilicate glass beads with a polymer that can be adjusted to modify the degree of cohesion. This method allows systematically varying the adhesive forces between particles, providing a versatile platform for experimental studies. The cohesion introduced through this approach remains consistent over time, and the adhesive force can be controlled by adjusting the thickness of the coating. The authors reported no dependence of the cohesion with the temperature in the range 20–60 °C. This stability is particularly beneficial for experiments that require reproducibility and precision, such as those investigating the flow properties of cohesive materials. Gans et al. measured the inter-particle force and reported an empirical expression for the adhesive force between two identical grains:40
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As discussed in Section 4, there exists a correspondence between the microscopic inter-particle force and the macroscopic cohesive stress. Gans et al. have used an inclined plane setup to investigate the friction and macroscopic cohesion of the CCGM. Their results, reported in Fig. 5(c) suggest that the yield stress of the material, τc and the microscopic cohesion force Fadh are related similar to what was reported for wet granular material τc ∼ Fadh/d2.40
Cohesion-controlled granular materials (CCGM) have been successfully used to study the erosion of a cohesive granular bed by a turbulent flow,86 and the collapse of granular columns,87,88 or the discharge of cohesive grains from a silo.89 Yet, some questions remain to be investigated to fully characterize this model material. In particular, how particle stiffness and tangential forces between particles are affected by the polymer coating remains unclear. Besides, preliminary rheological experiments at varying confining pressures have shown the coating can have effects on the inter-particle friction, in particular for thicker coatings,90 and this deserves detailed further study.
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| Fig. 6 Examples of (a), (b) magnetic and (c), (d) geometric granular cohesion. (a) Granular jet exiting a funnel in a cohesionless case (left), magnetic field parallel to gravity (middle) and perpendicular to gravity (right) [reproduced with permission from Lumay and Vandewalle,82 copyright 2008 American Physical Society]. (b) Examples of resulting collapse for different magnetic fields and particles [adapted with permission from Sunday et al.83 Copyright 2024 American Physical Society]. (c) Columns of 2.5 cm, 5 cm, and 10 cm wide hexapods [reproduced from Barés et al.84]. (d) Column of long thin rods (left) and staples (right) maintaining the shape of the container in which they were initially formed [reproduced from Franklin,85 with the permission of the American Institute of Physics]. | ||
This method has a few advantages: it is nonintrusive and not very sensitive to environmental conditions. Nevertheless, the granular flow generated using this method differs from typical flow dynamics, as cohesive forces align with the magnetic field, creating directional effects. Additionally, these forces are not evenly distributed around each particle, resulting in anisotropic attractions and repulsions within the material. Moreover, the intensity of the cohesion decreases rapidly with distance from the magnetic source, leading to inhomogeneous and time-varying cohesion as the particles move.
One of the first definition of geometric cohesion was given by Franklin,85 following some experiments of jamming97 and column collapse of rigid fibers of different aspect ratio.98 The interlocking of fibers can, for instance, prevent granular columns from collapsing, hence demonstrating a notion of cohesion. It also explains why an assembly of flexible fiber presents an elastoplastic response to compression. Interestingly, this notion of cohesion, and thus aggregates, was already observed with fibers by Philipse99 who reported that pouring fibers of very long aspect ratio out of a container produces a plug that retains its shape outside the container thus suggesting an apparent cohesive lengthscale that depends on the granular packing and interlocking.
Although this notion of cohesion is more complex as it involves a crucial role in the shape of the particles, different approaches have been considered to studying particles of concave shape on the static properties of the granular packing. Gravish et al. have shown, for instance, that U-shaped particles can form large-scale aggregates by entanglement.100 More recently, various studies have considered hexapod-shaped particles and explored how such particles can form column and free-standing structures thanks to the geometric cohesion,101–104 as well as studying the stress and force transmission.105,106
Few studies have considered flowing properties. Yet, Huet et al. have recently considered the avalanche dynamics of cross-shaped particles using a dam break setup and have shown that experimental results are harder to repeat due to the random nature of the entanglement.107 Their study also suggests the presence of mesoscale structures of granular networks of nonspherical particles, which can be seen as reminiscent of a cohesive length. In a rotating drum, Wang et al. have recently shown a regime where concave particles are flowing and one where the particles remain interlocked,108 and laid out a general framework for steady-state behavior.109 They introduced the notion of geometrical consistency to describe how when grains entangle, it causes the bulk material to resist flowing and effectively act as a cohesion.
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While the focus of this article is to review developments of controlled cohesion made through experiments, we should mention that discrete numerical simulations rely on this description. Various numerical models for Fadh have been developed and usually rely on a short-range attractive force between particles that rapidly decreases to zero when the grains are separated by an arbitrary distance.3,111,115,116 Different reviews and textbooks have summarized some numerical approaches, but cohesive forces used in both discrete element methods (DEM) as well as particle-resolved simulations within fluids often remain ad hoc, containing different assumptions, and are yet to be validated exhaustively.117–119
A key advantage of controlled-cohesion materials is the possibility of using large particles, of a few hundred microns to a few millimeters, which allows for more refined imaging than small powders. Furthermore, the large size of particles allows neglecting the effects of air drag, which introduces additional complexities, with respect to the other forces, as can be seen in Fig. 2(a) for particles larger than a few hundred microns. To make model cohesion at this scale, the adhesive force must have a magnitude larger or comparable with the weights of the particles.
Experimentally, the overall effects of cohesion can be increased by either increasing Fadh or reducing FW. The experimental techniques to control Fadh were discussed in Section 2. Using particles of the same density, tuning the particle size can be used to control the relative effects of cohesion, as shown in Fig. 1, since the weight and the different adhesive forces scale differently with the diameter of the particles. For instance, for capillary cohesion, Bog ∝ 1/d2, decreasing the diameter of the particles by two increases the relative effects of cohesion by a factor of four.
Characterizing adhesion using a granular Bond number is found to be particularly successful when processes are taking place at the scale of individual grains or bonds. These experiments can be categorized into two main kinds. First, where particles are being mechanically detached, and the effect of adhesion is to resist their separation.63,86 Additionally, adhesion modifies the mechanics at the contact affecting regular granular processes such as how particles accumulate into aggregates or piles, and spread.
Additionally, the effects of hydrodynamic forces on assemblies of grains can dislodge particles or, in the case of cohesive grains, erode clusters of particles.86,128 Experiments have been conducted where hydrodynamic forces are used to break bonds between particles from a granular assembly and cause them to be eroded and suspended. Such experiments provide a simple model for erosion. Experiments with both solid bridges,63 or polymer-coated CCGM86 have shown that a Bond number can be used to describe modifications on the onset of erosion due to cohesion. Erosion by the impact of other particles, modeled with sand-silicon oil mixtures is to well described by such a description.128,129 As expected intuitively, more cohesive grains are more resistant to erosion, and the delay in the erosion threshold can be quantified using the Bond number.
More generally, only a few experimental configurations exist that study the attachment of particles from individuals to clusters of particles of different shapes and sizes. The main experimental approach to study such clustering of particles is either by trapping them at an interface (the “Cheerios” effect)138–142 or by acoustically levitating them so as to minimize the effects of gravity.143–145 Experiments with the drop-by-drop accumulation of oil droplets – adhesive but frictionless – into a granular agglomerate or puddle have been shown to display continuum-like behavior.146,147
While a distance of about 10 grain diameters is often used as an order of magnitude used to delineate particle-scale and bulk-scale processes in cohesionless granular materials,32 a similar delineation has not been developed for cohesive grains. In particular, the distances over which the finite-size effects are present in cohesive granular media are expected to depend on the magnitude of cohesion.148,149 With the assumption that the effects of confinement are negligible, a framework of continuum mechanics is used to describe the material in terms of its relevant stresses.30–35
Often, the geometry of the granular assembly is also leveraged to only consider planar stresses, such that they can be represented using a Mohr circle. Derivations of the stresses in this formalism are widely available, for instance, in Nedderman.30 Combined with a Coulombic-frictional yield criterion, this provides the simplest description of failure and stability in a bulk granular material. For stability, any plane within a cohesionless granular material must have confinement stresses σ scaled by μs, to be larger than the tangential stresses on the plane τ, τ ≤ μsσ.11 The critical angle is related to the internal friction coefficient: tan
θc = μs. As a column confining a granular assembly is slowly lifted, the confined grains spread into such a sandpile. Experiments are shown in the top row of Fig. 1 for a range of grain sizes, initially filled with 350 g of grains, with aspect ratio a = Ho/Ro ≈ 4. Indeed, in the absence of cohesion, smoothed angles of the relaxed piles are very similar regardless of grain size, θc ≈ 22–23°, i.e. μs ≈ 0.4.
| τ ≤ μsσ + τc, | (6) |
Besides σc and τc, σt is also used to describe cohesion. All these three quantities are marked for a model yield locus in Fig. 7(b). The unconfined cohesive stress, σc is a measure of the systems own compression in the absence of confinement.30 This quantity is often used when compressive stresses are being discussed in the context of cohesive grains.31,150 The yield stress, τy, is used to describe the resistance of cohesive grains to shearing stresses.45 Finally, tensile stresses in the presence of cohesion are described in terms of the macroscopic tensile strength, σt.39 A set of indentation tests, that measure the tensile stress while lifting an indenter, initially compression into a granular bed have also been used to estimate σt.151 In the Mohr–Coulomb model, friction and cohesion are separated from each other, and consequently σt ∼ τc ∼ σc. One can readily see how such a description is useful when describing bulk processes. Importantly, such a description is independent of the source of cohesion between grains and is consequently useful to describe powders and soils, where the exact sources of cohesion may be hard to delimit. For the range of grains used in experiments with capillary bridges or CCGM, the cohesive stresses are usually of order a few hundred Pa.
An important purpose of making model cohesive granular materials is to be able to clarify the relationship between the particle- and macroscopic scale characterizations. From the tension-based experiments of particle–particle adhesion and using dimensional analysis, we expect σt ∼ Fadh/d2. Studies have shown that the value of the yield stress τc of mono-disperse wet granular material in the pendular regime,45 or cohesion-controlled granular material (CCGM)40 can also be estimated by relating it to the inter-particle force Fadh, with the same scaling. Rumpf's model enables estimating the macroscopic cohesion using a mean-field method for a homogeneous, isotropic granular medium composed of monodisperse grains while neglecting the effects of the inter-particle force distribution in the material.34,150,152–155 The yield stress of the material is then estimated as follows:45
![]() | (7) |
Cohesion is also sometimes characterized by a length scale, which is larger than the scale of the particle and which depends on the amplitude of the attractive forces. From scaling analysis, we expect a length-scale4,87–89
c ∼ σc/ρgg, | (8) |
It should be emphasized that a flow condition such as Mohr–Coloumb or Cam–Clay is regarding the onset of plastic deformation, and is generally studied in static or quasi-static conditions. Much less is understood systematically about cohesion in dynamic conditions. In the case of cohesion due to capillary bridges, for instance, when inertia is relevant to the deformation of an assembly, other effects, such as the viscosity of the liquid bridge or the lubrication due to the wetting fluid, can modify the apparent cohesion.156 Finally, the effects of cohesion are known to majorly affect how grains pack together, as large void spaces between grains can be left unfilled.157,158 Larger cohesion therefore result in smaller overall ϕ, thereby localizing other mechanical processes.
Additionally, a flowability or flow index159 is often constructed to gauge if a given powder will flow in a given situation.31,33f is described using a comparison of confinement pressure, σapplied, and the unconfined yield stress, σc. Rather than explain the general mechanics of some cohesive grains, such a description is unique to some experimental configurations. In the case that f ≡ σapplied/σc ≪ 1, the material is solid-like, and does not flow. For f ≫ 1, i.e., σapplied ≫ σc, the system flows freely as though it were cohesionless. In other words, cohesive granular materials can be made to flow under such conditions.
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| Fig. 8 (a) The free surface of a pile of grains, after a column of a = H/R = 5 is rapidly lifted for cohesionless (top) and cohesive grains (bottom) [adapted from Sharma et al.88 Copyright 2024 American Physical Society]. (b) The columnar collapse of a cohesive granular column (CCGM) of a = H/L ≃ 2 [adapted from Gans et al.87 Copyright 2023 Cambridge University Press]. (c) The collapse and unchannelized spread of a column a = 3 of dry and wetted grains [adapted with permission from Li et al.161 Copyright 2022 American Physical Society]. (d) A thin layer of grains, undergoing flexural bending between the two dashed lines, breaks at fixed wavelength [adapted with permission from Géminard et al.162 Copyright 2012 American Physical Society]. (e) Free surface on an inclined granular layer after the flow has stopped [reprinted with permission from Deboeuf and Fall.163 Copyright 2023, The Society of Rheology]. (f) The free surface of grains in a rotating drum for cohesionless (top) and CCGM for 1 rad s−1. All shown scale bars, unless specified, are 10 cm. | ||
Pakpour et al.42 provide an expression for the maximum height of a stable column, similar to an expression regarding the buckling of an elastic column, using similarly defined elastic properties for wetted grains. More recently, Gans et al.87 used CCGM and a length-scale-based description to show the critical height of rectangular columns using the cohesive length
c. It should be emphasized that the stability of a column is likely highly sensitive to its preparation. The overall packing of cohesive grains is substantially smaller than cohesionless grains, even if some agitation is provided to consolidate after raining in.164–166 Consequently, regardless of whether consolidation is provided externally or just due to the weight of the column itself, the average number of contacts may vary.167
In the same vein, while the maximum angles of stability for cohesive grains are similar in many experimental configurations, some variations are observed for each system. Initial experiments for the stable angle done through the crater left after drainage of wetted grains at the base of a container168,169 allowed for a prediction for the stable angle based on Mohr–Coulomb.11 The angle of repose has also been studied for a slowly lifting reservoir while measuring the angle of the slowly spreading pile by Samadani and Kudrolli.170 Gans et al.40 provided a few results on how the angle of repose of CCGM is modified when grains are released from a chute on a round plate. Nowak et al.148 have provided a framework to estimate the angle in a slowly rotating drum, as it also depends on the drum width. Altogether, larger amplitudes of cohesion lead to larger repose angles, while the precise prediction depends on the pile-making process. While cohesionless grains are smooth to the order of ∼1 d for all these measures of the repose angle, cohesion introduces roughness into deposits.
Additionally, experiments with cohesion have been interested in the collapse and spreading of columns of grains, where the confining boundaries are rapidly removed.171,172 These have been studied using both wetted grains and CCGM for a cylindrical column, spreading axisymmetrically88 (shown, e.g., in Fig. 8(a)); a rectangular column, spreading in a channel87,88,149,173–175 (shown, e.g., in Fig. 8(b)); a rectangular un-channelized geometry161 (shown, e.g., in Fig. 8(c)). In all cases, more cohesion leads to lesser overall deformation of the column. Some of these studies quantify the magnitude of cohesion for wet grains using the Bond number.161,173,175 The concentration of humidity W% = mliq/msolid plays a large role and is included alongside Bog to explain the range of results as shown by Artoni et al.173 Quantifying cohesion using the cohesive yield stress, τc, is shown to similarly systematize the spreading behavior of such systems.87,88,174 Indeed, such a description is not specific to the forces at the scale of the grain and has been shown for both CCGM and grains wetted with water cumulatively.88
Cohesive materials usually display roughness on their surfaces. Some examples are shown in Fig. 8(a)–(e). A number of studies have looked at the effects of a thin cohesive layer of grains subjected to stresses.151,162,176,177 Stretching such layers always leads to instabilities and the formation of patterns on the surface.151,176 In Fig. 8(d), we show results from Géminard et al.,162 where such a thin layer is flexed and undergoes successive fracturing. Further, using the growth of a model crack, Tapia et al.177 have shown how clusters, dependent on the magnitude of cohesion, control the breakup process. Similar successive structures are observed by Deboeuf and Fall163 once the flow of a cohesive granular material over a rough inclined plane has finished (shown, e.g., in Fig. 8(e)). Discontinuities are observed in the flowing states as well. Numerical simulations from Abramian et al.4 have also shown that roughness exhibited on the free surface after a column has collapsed may be characteristic of the magnitude of cohesion. Finally, grains being rotated in a cylindrical drum, as shown in Fig. 8(f) for CCGM, display a wide range of roughness dependent on the cohesion.
Besides their effect on free surfaces, the presence of cohesion is expected to modify other well-studied granular phenomena. The mass flow rate of grains discharged from a bin is reduced by cohesion and is found to depend on the cohesive length in a Beverloo-like relation.89 Similarly, some work on the measurement of drag in unsaturated wet sand178 and on the impact of projectiles onto beds of wetted grains179 has been performed, but additional studies in different geometries and with alternate cohesions need further consideration.
The variety of experimental techniques to make model cohesive granular materials, including capillary bridges, solid bonds, and polymer coatings, now pave the way to exciting development to account for cohesion in granular flow. In this article, we reviewed these different approaches and how they have been used to quantify macroscopic properties such as shear strength, yield stress, and cohesion-related length scales that reflect the effects of interparticle forces. This experimental progress should allow the development of more refined models that bridge particle-scale interactions with bulk material properties, thus offering a framework applicable to both industrial processes and natural phenomena where cohesive particles are significant. In addition, some approaches using cross-linked polymer microparticles are now considered to customize the surface properties in particulate suspensions.180
Future research will be able to leverage model cohesive grains to further elucidate different effects of cohesion, such as on the packing density and homogeneity, flow behavior, and responses under various stress conditions. Studies on aging, consolidation, and creep behaviors should be considered, as these time-dependent phenomena introduce complex length-scale dynamics and hysteresis effects that remain underexplored.181,182 In addition, it remains important to establish methods to correlate inter-particle forces with bulk mechanical properties to further enhance modeling approaches for the design and handling of cohesive materials. The dynamics of collisions, breakups, and particle exchange in cohesive systems are still poorly understood, especially for polydisperse and heterogeneous systems where particles have varying degrees of cohesion. For instance, experiments on cohesive particles of varying adhesion could improve our understanding of segregation phenomena.183 Additionally, cohesive rheology remains an exciting avenue for developing continuum models,3,87,184,185 such as the μ(I) rheology for cohesionless grains, which relates the shear stress τ to the pressure P acting on a granular material element through a macroscopic friction coefficient μ(I) =τ/P, where I is a measure of the system inertia.22–24I also controls the volume fraction, ϕ. How such rheological descriptions are modified due to inter-particle adhesion has so far only been studied using numerical simulations.3 Experimental systems with controlled inter-particle forces also provide valuable benchmarks for numerical simulations, including discrete element methods, enabling comparisons across different cohesion sources and particle types.
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