Overcoming paradoxes of Drucker-Prager theory for unconsolidated granular matter. (Dated: January 23, 2014)
|
|
- Stephen Evans
- 5 years ago
- Views:
Transcription
1 Overcoming paradoxes of Drucker-Prager theory for unconsolidated granular matter (Dated: January 23, 2014) 1
2 Abstract Drucker-Prager model of granular matter contradicts to experiments in several aspects some of which are quite "annoying", like, for example, the steady shear paradox: in a steady simple shear ow the continuum extends inde nitely in the direction normal to the ow. In this paper we discuss modi cations of Drucker-Prager model, which eliminate most obvious paradoxes while the most essential feature of the model, its simple variational structure, is preserved. Keywords: granular material, Drucker-Prager, dissipation minimization, fast granular ow I. INTRODUCTION Granular matter exhibits the features of gases, liquids and solids. The development of a conceptually simple continuum model capturing most of these features remains a challenge. The e orts go from two opposite sides: some start from mechanics of a dilute dissipative system of rigid colliding particles and increase density to allow the system to get to the jamming state, others begin with models of elasto-plastic continua and complicate these models to mimic dissipative particle ows. Another source of ideas stem from an analogy between granular ows and ows of molecules in deformed glassy metals. Over the years several indepth reviews of the subject have been given (Savage 1984, Campbell 1990, Nedderman 1992, Mehta 1994, Herrmann 1995, Jaeger et al. 1996, de Gennes 1999, Kadano 1999, Goldhirsch 2003, GDR MiDi 2004, Forterre et al. 2008, Goddard 2012). This relieves us of the necessity to present here a detailed overview, and we will mention further only the papers that are most relevant to our work. Modeling of granular matter was put on the solid ground of continuum mechanics by D.C. Drucker and W. Prager (1952). They suggested to treat bearing capacity of soil masses by a simple model of rigid-plastic body. Drucker-Prager model is based on the associated rule which, in fact, means that the model can be formulated as a minimum principle for rateindependent dissipation. A remarkable feature of Drucker-Prager model is that it establishes a link between friction coe cient and dilatancy of sheared granular matter, the phenomenon rst noticed and studied by Reynolds (1885). Here, however, comes a contradiction to experiments: the observed values of dilatancy appear to be smaller than predictions of 2
3 Drucker-Prager model. We call this further the friction coe cient paradox. There are other inconsistencies with experimental observations as well, they are discussed in Section 3. The inconsistencies led to abandoning the associated rule, and most models developed further do not possess a variational structure (Abaqus Drucker-Prager-Cap model, Spencer 1964, Goddard 1984, 1986, 2010, Vardoulakis et al. 1991, Gudehus 1996, Anand et al. 2000, Bocquet et al. 2001, Aranson et al. 2002, Bazant 2006, Jop et al. 2006, Khain et al. 2006, Kamrin et al. 2007, 2007, Khain 2007, 2011, Kamrin 2010, Andrade et al. 2012). A noticeable exception is Cam clay model and the critical state theory (Wood 1999). Our goal is to change Drucker-Prager model to get rid of the most obvious contradictions to experiments and preserve the most essential feature of Drucker-Prager model, its variational structure. The equations governing slow motion of granular matter should follow from minimization of dissipation for a simple reason: Since inertia is negligible while particle impenetrability and friction determine micromotion, the particles move to minimize dissipation. For fast owing granular matter a possibility to obtain the governing equations by dissipation minimization is less obvious. However, as will be seen further, the relations obtained for this case previously, also follow from minimization of the dissipation after an appropriate modi cation. In the next Section we describe Drucker-Prager model and in Section 3 its paradoxes. Then we modify the dissipation of Drucker-Prager model (Section 4), derive the corresponding constitutive equations (Section 5), nd velocity eld in Couette ow (Section 6), discuss the resolution of paradoxes (Section 7). Finally, we incorporate fracture of grains in Section 8, introduce a simple model with smooth dissipation in Section 9 and discuss the modi cations of previous theories rendering their variational structure in Section 10. In the concluding Section 11 it is formulated the main outcome of the paper, a simple model of granular matter that are free of the paradoxes of Drucker-Prager theory. II. DRUCKER-PRAGER MODEL Drucker-Prager model is a model of rigid-plastic body. First, we brie y outline the theory of rigid-plastic bodies. Rigid-plastic bodies. The central concept of the theory of rigid-plastic bodies is that not 3
4 all values of stress tensor components ij are possible: in the six-dimensional space of ij the admissible stresses lie within some convex region described by an inequality f ( ij ) 6 0: (1) If f ( ij ) < 0; then continuum does not move. If ij are on the boundary, f ( ij ) = 0; (2) then motion may occur or may not occur. If it does occur, then the strain rate e ij e ij = j i (3) u i being velocity eld, is linked to the stress tensor by the associated law e ij : (4) Parameter is determined by the entire boundary value problem which includes the equilibrium j = 0 (5) and prescribing surface force or velocity at the boundary of the body. If only surface forces are known, remains undetermined and the process can go with any rate; prescribing boundary velocity on a part of the boundary speci es the process rate. In (5) and in what follows summation over repeated indices is implied. We denote the region f ( ij ) 6 0 by ; the reason for supplying with index will be come clear further. Formula (4) makes sense for smooth functions f ( ij ) : Another assumption was that the region is to convex. If is strictly convex, then, formula (4) establishes a one-to-one correspondence between stresses and strain rates up to a factor : If the conditions of strict convexity and smoothness are not satis ed, then (4) must be recti ed. This is done by Drucker postulate, the maximum principle for the dissipation density D = ij e ij : for given e ij the stress state is determined by the variational principle D (e ij ) = max ij 2 ije ij : (6) 4
5 For smooth functions f ( ij ) and convex (4) follows from (6). For non-smooth functions f ( ij ) and/or not strictly convex the one-to-one correspondence of ij and 1 e ij is lost. For a given e ij there might be di erent ij maximizing dissipation, and one maximizer may correspond to di erent e ij : Variational principle. The beauty of Drucker postulate is that the entire theory of rigidplastic bodies gets a variational form. To formulate the corresponding variational principles, it is convenient to write (6) introducing function 0 D ij 2 ( ij ) = +1 ij 2 : (7) Then D (e ij ) = max ij (e ij ij D ( ij )) ; (8) For convex ; function D ( ij ) is also convex, and the relation that is inverse to (8) is true D ( ij ) = max e ij ( ij e ij D (e ij )) : (9) We see that D is the Young-Fenchel transformation (usually marked by *) of D: If D (e ij ) is strictly convex, there is only one e ij corresponding to a given ij : Drucker-Prager model. Drucker-Prager model corresponds to the special choice of function f ( ij ) : f ( ij ) = 0 ij 0 ij Here 0 ij is the deviator of the stress tensor a ii a 1 : (10) ij = p ij + 0 ij; p = 1 3 ii; (11) ij the Kronecker delta, a and a 1 are positive constants, p pressure. Formula (1) with function f (10) is a generalization of Mohr-Coulomb s friction law for continuum: at each cut friction force does not exceed normal force times friction coe cient k. Parameter a 1 in (10) is responsible for the cohesion: shear stress required for simple slip must not be smaller some cohesion stress. Zero a 1 corresponds to unconsolidated granular matter. Further we focus on that case. Parameter a 1 can be also set to zero for consolidated granular materials if cohesion is negligible in comparison with pressure. The region for a 1 = 0 is a cone with the vertex at the origin ij = 0: This region is not strictly convex, therefore, there is no one-to-one correspondence between ij and e ij when the material moves. 5
6 The relation between the friction coe cient k and the coe cient a can be established by considering two-dimensional stress states ( 13 = 23 = 0) with the condition for 33 inherited from the incompressible elasticity 33 = p or 0 33 = 0: Then p = ( ) =2; while the condition that at every cut shear stress does not exceed k times normal stress yields 0 ij ij 6 p 2 sin p; (12) where friction angle is de ned in terms of the friction coe cient as k tan : (13) Comparing (12) and (10) one gets a = p 2 sin : (14) One can show that at every cut the admissible surface forces are compressive, as one would expect for unconsolidated granular matter, if a 6 3 p 6: According to (14), this feature holds for any : In particular, pressure p cannot be negative; this follows also directly from (12). Further we call by Drucker-Prager model a special case of the rigid-plastic body with admissible stresses selected by condition (12). The cone has the singularity at ij = 0: A remarkable consequence of that is that admissible strain rates also can be only inside some conjugated cone in the six dimensional strain rate space: it turns out that dissipation density D (e ij ) de ned by (6) is equal to +1 if e ij are outside of ; i.e. such e ij are not realizable. Indeed, calculation D (e ij ) for admissible stress (12) yields: Here e and e 0 ij respectively: p 0 e > a e 0 D (e ij ) = ij e 0 ij +1 e < a p : (15) e 0 ij e0 ij are the rst invariant of the strain rate tensor and strain rate deviator, e = e ii = div! u ; e 0 ij = e ij 1 3 e ij: Further for brevity we denote the shear rate, the square root of the second invariant of strain rate deviator, by e 0 : e 0 = q e 0 ij e0 ij : 6
7 In nite dissipation in (15) means that there is a one-side constraint: some strain rates are prohibited. Namely, if shear rate e 0 is not zero, the volume increase rate e cannot be too small: e > ae 0 : (16) First of all, continuum cannot decrease its volume, and can only expand. Second, any shear causes volume increase. Such a picture is quite consistent with the behavior of an ensemble of close-packed rigid particles. Dilation of a sheared set of close-packed particles was rst theoretically and experimentally established by Reynolds (1885). Strikingly, as Drucker- Prager model claims, the volume rate of a sheared ensemble of particles, which is a purely geometrical parameter, is linked by (16), (14) and (13) to the friction coe cient k. In Drucker-Prager model the dissipation in owing particle ensemble is always zero. If e > ae 0 ; i.e. volume grows faster than it must do due to shear, particles loose the contacts, and dissipation must be zero indeed. If e = ae 0 ; then zero dissipation means that the power of shear stresses, 0 ije 0 ij; is equal to the power of pressure, pe. Let the granular material be subject to surface force density f i at a part of material f ; and another part of the u have a prescribed velocity u (b) i : Then the true velocity eld minimizes the dissipation functional Z Z I(u) = D (e ij ) dv f i u i da: f Due to (15), it is enough to consider the velocity elds for which div! q u > a e 0 ij e0 ij (17) while the dissipation functional is equal to I(u) = f f i u i da: (18) The true velocity eld minimizes the functional (18) on the set of all velocity elds obeying the constraint (17) and the constraint u i = u (b) i u : (19) 7
8 This problem is set at each instant t. Apparently, if u (b) i 6= 0; the region V changes in the course of motion. This type of variational problems has been discussed in much detail by Mosolov and Miasnikov (1981). The minimum value in the variational problem (18)-(19) can be there is no a nite velocity eld obeying to all equations, i.e. applied load. 1: This means that material cannot carry the The problem (18)-(19) is not strictly convex and may have many solutions. To select a unique solution the problem must be regularized. One of possible regularizations is the inclusion of viscous dissipation, Z I = V e ij e ij dv f f i u i da: (20) A unique solution is selected by taking the limit solution that corresponds to vanishing viscosity,! 0: Formally, the equations of Drucker-Prager model can be obtained by including the constraint (17) by means of Lagrange multiplier p: Z q I(u) = p a e 0 ij e0 ij div! u Varying functional (21) one gets V dv f f i u i da: (21) e 0 ij ij = app e 0 mn e 0 mn p ij ; (22) equilibrium equations (5) and usual boundary conditions of continuum mechanics. Hence, p has the meaning of pressure. One can show that at the minimizer pressure can be only non-negative. III. PARADOXES OF DRUCKER-PRAGER MODEL Here we summarize the most annoying contradictions of Drucker-Prager model to experiments. Steady shear paradox. Consider a steady homogeneous shear with velocity eld u x = _y; _ = const: (23) 8
9 Then and from (16) Hence, for _ 6= 0; u z = 0; u y = u y (x; y) : e ; e0 xx = 1 3 e; e0 zz = 1 3 e; e0 yy = 2 3 e; e0 xy = > 3a s 1 2 _ > 0 : and material expands inde nitely in the direction normal to the ow direction. The dilation is expected at the beginning of the ow, which started from a close-packed state. However, after the initial dilation, the material ceases to dilate further, and a steady ow must settle with no further volume change. Boundary layer paradox. In Couette ow one observes boundary layers near the moving boundaries. The thickness of the boundary layers is of the order of several grain diameters. To exhibit such a boundary layer, a continuum theory should contain a material characteristic with the dimension of length. The only material characteristic in Drucker-Prager model, a, is dimensionless. This makes Drucker-Prager model incapable of describing the boundary layers. Friction coe cient paradox. According to (16) and (14), nonzero shear rate causes some volume rate, and e e 0 = p 2 sin : (25) Observable values of e=e 0 are smaller (Spencer 1964). This constitutes the friction coe cient paradox. There are less disturbing issues with Drucker-Prager model, like, e.g., the absence of hysteresis in loading/unloading, but we focus further on resolving only the three ones described. Though the above-mentioned paradoxes diminish the applied value of Drucker-Prager model, its fundamental role as one of the benchmarks of granular material phenomenology is undeniable. 9
10 IV. MODIFICATION OF DRUCKER-PRAGER MODEL A modi cation of Drucker-Prager model considered here is based on the following physical reasoning. If a granular matter moves, the volume concentration of grains c evolves and obeys the equation of conservation of grain volume Here d=dt is the material time derivative dc dt + c div! u = 0: (26) d dt dt + i i In random packing of grains, c takes values in some range c jam 6 c 6 c max 6 1: (27) Parameters c jam and c max are the material characteristics. The low limit c jam is de ned as such value of c that for c < c jam grains are not in contact with overwhelming probability. In other words, for c < c jam the granular matter is uidized. The existence of the upper limit c max in random packing was established experimentally (see review by Forterre et al. (2008)). Emphasize that the maximum concentration in random packing c max is smaller than the maximum possible concentration. For example, for random packing of rigid spheres c jam 0:55; c max 0:64; while the maximum possible concentration is 0:74; it is achieved on hcp and bcc periodic packing. We assume that the microstructure is isotropic, and accept that the only essential macroscopic parameters of microstructure are the grain volume concentration c and the averaged grain diameter d. If d was not included, then the de nition of c jam given above could be meaningless. Indeed, for a given c jam < c < c max ; one can take a close-packed con guration with a concentration c 0 > c: Let us take this con guration and reduce diameters of all particles without changing their positions. Then particles loose the contacts. The new radii can be chosen in such a way that the new concentration is c. So, we construct a grain microstructure with concentration c and particles that are not in contact. Including average grain diameter in the set of macroscopic characteristics eliminates such microstructures. It 10
11 FIG. 1: Symbolic plots of dissipation density in Drucker-Prager model. remains unclear how wide is the set of available grain con gurations for a given c and d and how massive is the subset with non-touching particles. We assume that such subset, if exists, does not a ect considerably the grain ow dynamics. The mechanisms of deformation in the loose-packed grains could be similar to that of glassy metals at low temperature (see Kamrin and Bouchbinder (2013)). Limiting the characteristics of microstructure by only two numbers, c and d, we ignore, for example, the e ects of grain microstructure "fabric", which is of tensorial nature. The goal here is to outline the logic structure of the approach; further complications of our model incorporating the anisotropic features of the ow can be done within the same framework. Consider dissipation in Drucker-Prager model. A symbolic plot of Drucker-Prager dissipation is shown in Fig.1. Emphasize that dissipation is zero for e=e 0 = a: D (e; e 0 ) = 0 if e = ae 0 : (28) For any e=e 0 < a; dissipation is +1: The rst point of departure from Drucker-Prager model is the assumption that parameter a is associated not with the friction coe cient but with Reynolds dilation: if e 0 6= 0; then the material must dilate with some rate e > ae 0 ; otherwise the grains fracture (incorporation of grain fracture is considered further in Section 9). Prohibiting the volume rates e < ae 0 corresponds to setting D = +1 for such rates. The dilation coe cient is a a pure kinematic characteristic of the granular microstructure. In principle, it is not related to the friction coe cient. The friction coe cient a ects the values of dissipation. 11
12 FIG. 2: Typical dependence of a on c: Our next deviation from Drucker-Prager model is the assumption that a may depend on c: e > a(c)e 0 : One can expect that a(c) decays with c, and vanishes at c = c jam (Fig. 2), i.e. at c = c jam for arbitrary small shear rates, the volume can increase with any rate, while the volume decrease is prohibited: e > 0: The general form of dissipation D for granular materials can be established from dimension reasoning. Apparently, the parameters on which D may depend on are: ; d; e; e 0 ; c; (29) being the grain mass density. We do not mention explicitly the friction coe cient, which is dimensionless. From theorem where D 0 (e=e 0 ; c) is a dimensionless function. D = d 2 e 03 D 0 e e 0 ; c Consider rst deformation of granular material in the close-packed range of concentrations, c jam 6 c 6 c max : It is natural to assume that deformation in this range is rate independent, i.e. the work done to deform granular mass does not depend on the rate of deformation. For rate independent deformations, dissipation must be a homogeneous function of the rst order. Obviously, function (30) can be such a function only if D 0 is equal to zero or in nity, as in the case of Drucker-Prager model. We consider rst the most simple possibility and set for c jam 6 c 6 c max D = (30) 0 a(c)e 0 e a(c)e 0 e > 0 : (31) 12
13 FIG. 3: Characteristic regions in (c; e=e 0 ) plane. For c < c jam the granular matter is uidized and behaves as a nonlinear viscous uid. The uid is nearly incompressible, therefore, the parameter e=e 0 is small. Expanding D 0 in Taylor series for small e=e 0 and keeping only the rst two terms we have D = 3 d2 e 03 1 e e 0 : (32) Parameters and may depend on c. Parameter is positive because the larger e the smaller dissipation must be (particles y away and the number of collisions drops). Parameter is, obviously, positive as well. Function (32) must be modi ed for nite e=e 0 to warrant positiveness of D. In such modi cation D should be decaying function of e=e 0 : We set D = 3 d2 e 03 e e=e0 : (33) Presumably, this relation holds in a small vicinity of the point c jam : c. c jam : The dissipation introduced is discontinuous. This is natural, because granular materials experience solid-like phase transitions. The lines of discontinuity are shown in Fig. 3. There are three characteristic regions in the (c; e=e 0 ) plane. In the transition from c < c jam to c > c jam uid-like behavior changes to solid- uid one. Similar is the transition across the line e=e 0 = a(c) for c > c jam : The essential di erence between the states with c < c jam and c > c jam is that for c > c jam dissipation due to collisions is practically absent. Dissipation discontinuities does not cause di culties in setting the variational problem. Regularization 13
14 can be done by means of vanishing linear viscosity. Further in Section 9 we discuss a way to smooth dissipation. V. CONSTITUTIVE EQUATIONS The governing equations of the model follow from minimization of dissipation functional, Z Z I = D (e 0 ; e; c) dv f i u i da; (34) f over velocity elds for each time instant. Regularization of this functional, if needed, can be done by vanishing viscosity as in Section 2. Typically the minimizing velocity eld is zero in some subregion V 0 of V; a rigid core, and nonzero outside of V 0 : A simple way to obtain the constitutive equations is to vary strain rates e ij and velocities ui that are subject to constraints (3). Denoting Lagrange multipliers for these constraints by ij, we obtain the functional Z V D (e 0 ; e; c) ij e ij j dv i f f i u i da: (35) In accordance with Lagrange multiplier method (see e.g. Berdichevsky 2009, Sect. 5.10), functional (35) must be minimized over e ij and u i and maximized over ij. Minimization over u i yields the equilibrium equations (5) and natural boundary conditions. Minimization over e ij is a local problem that should be done at each space point min e ij (D (e 0 ; e; c) ij e ij ) : (36) Split of stress tensor in its deviator and spherical parts renders a more convenient form of the variational problem (36) min D (e 0 ; e; c) 0 ije 0 e 0 ij ;e ij + pe : (37) It is easy to see that, for a known e 0 ; e 0 ij is determined from the equation e 0 ij e 0 q = 0 ij ; 0 0 = 0 ij 0 ij (38) 14
15 while e 0 and e should be found from the minimization problem min [D (e 0 ; e; c) 0 e 0 + pe] : (39) e;e 0 In case of the model described in the previous Section, (39) yields the following constitutive equations: if c jam 6 c 6 c max ; then, for each c, Drucker-Prager equations hold; if c < c max ; For small e=e 0 (40) simpli es to 0 = d 2 e e e 0 3 e 0 = 3 d2 e 02 e e=e0 : (40) 0 = d 2 e 02 p = 3 d2 e 02 : (41) These are the equations we will use in the next Section, because, as was mentioned, steady uidized granular motion is approximately incompressible. VI. COUETTE FLOW Consider a simple ow geometry shown in Fig. 4: granular matter is con ned between two walls; the bottom wall does not move, the upper wall moves with velocity U along x axis; ow is unbounded in x, z directions; upper wall can move in y direction and loaded with normal surface force density P, stresses in x, z directions, xx and zz ; are also equal to P. We are going to nd the ow using the model of Section 5. Stresses are constant over space coordinates xx = yy = zz = P; xy = const thus p = P: In steady regime only u x is nonzero, u x = u x (y) ; and e = 0; e 0 = ju x;y j p 2 : From (41) p = (c)(c) d 2 u 2 x;y = P; (42) 6 15
16 FIG. 4: Geometry of Couette ow. 0 = p 2 j xy j = (c)d 2 u 2 x;y. 2 = const: (43) In general, u x;y and c may depend on y: This dependence is determined by the history of the wall acceleration. We consider a simpler case when does not depend on c: Then, from (43), u x;y is a constant, and from (42), c is a constant as well. If the thickness of the ow region is h, then u x;y = U=h: In the rigid core, 0 = p 2 j xy j 6 a P: Assuming that motion started from a random close-packed state with concentration c 0 ; we obtain the value of xy ; Then ju x;y j = Consistency of (45) yields the equation for c: Then equation (42) determines the thickness of ow region j xy j = a (c 0) p 2 P: (44) s s 2a (c 0 ) P 6P = d 2 (c) d : (45) 2 (c) = 3 a (c 0 ) : (46) U 2 h = 6P 2 (c) d : (47) 2 The thickness of the boundary layer is of the order of grain size d; as expected. As follows from (42), (43), the friction coe cient k is k = j xyj p 16 = 3 p 2 :
17 Function (c) is expected to be a growing function of c, taking its maximum value at c = c jam : A solution of equation (46) exists as long as 3=a (c max ) < (c jam ) and c 0 is su ciently close to c max : If c 0 is close to c jam (the random packing is very loose), then solution of (46) does not exist for 3=a (c 0 ) > (c jam ) : In other words, in shear ow su ciently loose packing dissolve and do not form a rigid core. Absence of data on Reynolds dilation does not allow for quantitative analysis of this problem. VII. DISCUSSION OF PARADOXES As the solution of Couette problem shows, our model exhibits boundary layers with the thickness of the order of grain size as it must be. Apparently, the steady shear paradox is also resolved: volume increases until a becomes zero, and, accordingly, steady shear with no volume change becomes possible. The situation with the friction coe cient paradox is less clear. This can be reexamined after the model parameters are experimentally determined. VIII. INCORPORATION OF GRAIN FRACTURE Grain fracture was prohibited by the volume rate constraint e > ae 0 : If grains fracture, e can be less than the low limit ae 0 required by geometry of rigid grains. Accordingly, dissipation is nite for e < ae 0 : We mention here a simple model when dissipation becomes a linear function of e=e 0 in the entire region e 6 ae 0 : { (ae D (e 0 0 e) ae 0 ; e; c) = 0 ae 0 e > 0 e 6 0 : (48) Here { and a are some functions of c. The admissible stresses in such model are in the region 0 6 p 6 {; 0 6 ap: This region is shown in Fig. 5. If 0 < p < { and 0 < ap, then If p = { and 0 < ap; e = e 0 = 0: e < 0; e 0 = 0: 17
18 FIG. 5: Admissible stresses. If 0 < p < { and 0 = ap, e = ae 0 : If simultaneously p = { and 0 = ap; then vector fe; e 0 g is a linear combination with positive coe cients of two vectors f 1; 0g ; and f1; ag : This model is reminiscent of Abaqus Drucker-Prager-Cap model with one essential di erence: it has a variational structure and the associate rule is respected. IX. SMOOTHING THE DISSIPATION If fracture and non-elastic deformation of grains are possible, like in soils, then for c jam 6 c 6 c max dissipation can be nite and non-zero for both e < ae 0 and e > ae 0. A simple generalization of the model of Section 4 is to set for all c D = (c) 3 d2 e 03 e (c)(a(c) e=e0) : (49) Here, as before, a (c) characterizes Reynolds dilation; a (c) is extended by zero for c < c jam : Function (49) is a continuous function of strain rates. Solid- uid transition is associated with vanishing of a (c) at c = c jam and possible discontinuities of (c) and (c) at this point. The model of Section 4 is obtained by tending (c) to in nity for c > c jam : 18
19 X. ON FAST GRANULAR FLOWS Over last two decades considerable e orts were focused on developing equations of granular matter starting from gaseous phase and increasing grain concentration until jamming (Savage 1998, Losert et al. 2000, Bocquet et al. 2001, Garcia-Rojo et al. 2006, Khain et al. 2006, Khain 2007, 2011, Luding 2009, Otsuki et al. 2010). In this Section we show that some models suggested in this eld can be obtained from minimization of dissipation if some simplifying assumptions are made. The granular gas/liquid continuum is characterized, in addition, to grain concentration c and velocity, by granular temperature T (average squared velocity uctuation), and the closed system of equations consist of continuity equation (24), momentum equation energy equation constitutive equations for stress tensor and "heat ux" q i ; du i dt j ; (50) dt dt = ijv i;j q i;i T 3=2 (51) ij = p ij + 1 e ij + 2 ij ; p = p 0 T q i = T ;i : (52) The last term in (51) describes the energy loss due to non-elastic collisions of grains. From dimension reasoning, viscosities 1 ; 2 and "heat conduction" are proportional to T 1=2 : 1 = 1 d p T ; 2 = 2 d p T ; = 0 d p T (53) while = 0 =d; where 1 ; 2 ; 0 ; 0 are dimensionless functions of c. When c approaches c jam all these parameters diverge, presumably as (c jam c) 1 : These equations are rmly established in the limit c! 0 by an asymptotic analysis of Boltzmann equation incorporating inelasticity of particle collisions (Sela et al. 1996, 1998, Goldhirsch 2003). For c being closed to c jam these are pure phenomenological equations. 19
20 The equations do not have a variational structure even for quasi-static motion, when one neglects the left hand sides in (50) and (51). The situation changes if for quasi-static motion the "heat ux" in energy equation can be neglected, and motion is nearly incompressible (e 0) : Indeed, plugging (52) and (53) in (51) one nds temperature: T = function of c d 2 e 02 : Then viscosity becomes while 1 = function of c d 2 e 0 p = function of c d 2 e 02 (54) 0 ij = function of c d 2 e 02 e0 ij e 0 : (55) Equations (54), (55) can be obtained from minimization of dissipation D = 1 3 d2 e 03 e e 2 e + : (56) 0 e 0 Here the coe cients are positive functions of concentration. The sign minus in the second term is caused by decrease of dissipation for ying out grains (e > 0) : The last term is added to avoid negativeness of dissipation for large e, but the model makes physical sense only for small e. For small e=e 0 (54), (55) coincides with the constitutive equations of Section 5 (41). Note an apparent aw of using dissipation (56): pressure p becomes negative for su ciently large e=e 0 ; while an unconsolidated granular matter does not withstand negative pressure. Dissipation (33) is free from this defect. Equations (54), (55) can be presented in another form. As follows from (54) and (55) 0 ij p = e0 ij e 0 ; (57) being a function of c. Equation (54) can be written in terms of inertial number, I = e0 d p p= ; as 1 = function of c: (58) I2 20
21 Equation (58) can be solved with respect to c, and c becomes a function of inertial number. Plugging this dependence in (57) we arrive at Jop-Forterre-Pouliquen constitutive equation (Jop et al. 2006): 0 ij p = (I) e0 ij e 0 (59) where (I) is a prescribed function of I. Equation (59), was complemented by the incompressibility condition div! u = 0: (60) Together with equilibrium equations (5) these equations form a closed system of equations. Unfortunately, such setting has a aw: pressure is a required function of space coordinates, which is determined by the solution of a boundary value problem. In principle, pressure found from the boundary value problem might be negative. Besides, concentration is constant due to (60), and back path to (54), (55) is lost. Equations loose also the variational structure. The form of equations for liquid phase (54), (55) seem preferable. XI. CONCLUSION The main outcome of the paper is a simple model of granular matter formulated in Section 9. Here we present it in the form of a variational principle: Consider region V (t) occupied by a granular media. The values of velocity are given at the (t) of V (t) : u i = u (b) i (t): (61) Let the current volume concentration of particles of a granular media be c(t; x): Then at each instant t the true velocity eld minimizes the dissipation functional Z 1 3 (c)d2 e 03 e (c)(a(c) e=e0) dv where V (t) e q i ; e 0 = e 0 e0 ij ; e0 ij = i j 1 i 3 e ij while functions (c) ; (c) and a(c) are material characteristics, the features of which are described in the text; d 2 is a constant factor with the dimension mass density times length 21
22 squared making (c) dimensionless. Evolution of c(t; x) is determined by the + div(c! u ) = 0: As shown in the text, this model is reduced to Drucker-Prager model by an appropriate limit procedure. In general, the model is rate-dependent, and, for an appropriate choice of (c), includes grain fracture and the corresponding creep. References 1. Anand, L., and C. Gu, Granular materials: constitutive equations and strain localization, J. Mech. Phys. Solids, 48, 1701 (2000) 2. Andrade, J.E., Chen, Q., Le, P.H., Avila C.F., and T.M. Evans, On the rheology of dilative granular media: bridging solid-and- uid-like behavior, J. Mech. Phys. Solids, 60, (2012) 3. Aranson, I.S., and L.S. Tsimring, Continuum theory of partially uidized granular ows, Phys. Rev. E, 65, (2002) 4. Bazant, M.Z., The spot model for random-packing dynamics, Mech. Mater., 38, 717 (2006) 5. Berdichevsky, V.L., Variational principles of continuum mechanics, Springer, Bocquet, L., Losert, W., Schalk, D., Lubensky, T.C., and J.P. Gollub, Granular shear ow dynamics and forces: Experiment and continuun theory, Phys. Rev. E, 65, (2001) 7. Campbell, C.S., Rapid granular ows, Annu. Rev. Fluid Mech., 22, 57 (1990) 8. Drucker, D.C., Prager, W., and H.J. Greenberg, Extended limit design theorems for continuous media, Q. Appl. Math., 9, 381 (1952) 9. Drucker, D.C., Limit analysis of two and three dimensional soil mechanics problems, J. Mech. Phys. Solids, 1, 217 (1953) 22
23 10. Forterre, Y., and O. Pouliquen, Flows of dense granular media, Annu. Rev. Fluid Mech., 40, 1-24 (2008) 11. de Gennes, P.G., Granular matter: a tentative view, Rev. Mod. Phys., 71, s374 (1999) 12. Garcia-Rojo, R., Luding, S., and J.J. Brey, Transport coe cient for dense hard-disk systems, Phys. Rev. E, 74, (2006) 13. GDR MiDi, On dense granular ows, Eur. Phys. J. E, 14, (2004) 14. Goddard, J.D., Dissipative materials as models of thixotropy and plasticity, J. Non- Newtonian Fluid Mech., 14, (1984) 15. Goddard, J.D., Dissipative materials as constitutive models for granular media, Acta Mech., 63, 3 (1986) 16. Goddard, J.D., Parametric hypoplasticity as continuun model for granular media: from Stokesium to Mohr-Coulombium and beyond, Granular Matter, 12, 145 (2010) 17. Goddard, J.D., Playing in sand for engineering, science and fun, G.I. Taylor Award Lecture, Goldhirsch, I., Rapid granular ows, Annu. Rev. Fluid Mech., 35, (2003) 19. Gudehus, G., A comprehensive constitutive equation for granular materials, Soils and Foundations, 36, 1-12 (1996) 20. Herrmann, H.J., Physics of granular media, Chaos, Solutions & Fractals, 6, 203 (1995) 21. Jaeger, H.M., Nagel, S.R., and R.P. Behringer, Granular solids, liquids, and gases, Rev. Mod. Phys., 68, 1259 (1996) 22. Jop, P., Forterre, Y., and O. Pouliquen, A constitutive law for dense granular ows, Nature, 441, 727 (2006) 23. Kadano, L.P., Built upon sand: Theoretical ideas inspired by granular ows, Rev. Mod. Phys., 71, 435 (1999) 23
24 24. Kamrin, K., Rycroft, C.H., and M.Z. Bazant, The stochastic ow rule: a multi-scale model for granular plasticity, Model. Simul. Mater. Sci. Eng., 15, 449 (2007) 25. Kamrin, K., and M.Z. Bazant, Stochastic ow rule for granular materials, Phys. Rev. E, 75, (2007) 26. Kamrin, K., Nonlinear elasto-plastic model for dense granular ow, Int. J. Plasticity, 26, (2010) 27. Kamrin, K., and E. Bouchbinder, Two-temperature continuum termomechanics of deforming amorphous solids, J. Mech. Phys. Solids (submitted), (2013) 28. Khain, E., and B. Meerson, Shear-induced crystallization of a dense rapid granular ow: Hydrodynamics beyond the melting point, Phys. Rev. E, 73, (2006) 29. Khain, E., Hydrodynamics of uid-solid coexistence in dense shear granular ow, Phys. Rev. E, 75, (2007) 30. Khain, E., Dense granular Poiseuille ow, Math. Model. Nat. Phenom., 6, 77 (2011) 31. Losert, W., Bocquet, L., Lubensky, T.C., and J.P. Gollub, Particle dynamics in Sheared granular matter, Phys. Rev. Lett., 85, 1428 (2000) 32. Luding, S., Toward dense, realistic granular media in 2D, Nonlinearity, 22, R101-R146 (2009) 33. Majmudar, T.S., and R.P. Behringer, Contact force measurements and stress-induced anisotropy in granular materials, Nature, 435, 1079 (2005) 34. Majmudar, T.S., Speri, M., Luding. S., and R.P. Behringer, Jamming transition in granular systems, Phys. Rev. Lett., 98, (2007) 35. Mechta, A., and G.C. Barker, The dynamics of sand, Rep. Prog. Phys., (1994) 36. Mindlin, R.D., and H. Deresiewicz, Elastic spheres in contact under varying oblique forces, J. Appl. Mech., 20, 327 (1953) 24
25 37. Mosolov P.P., and V.P. Miasnikov, Mechanics of rigid-plastic media, Moscow, Nauka, (1981) 38. Nedderman, R.M., Statics and kinematics of granular material, Cambridge Univ. Press, (1992) 39. O Hern, C.S., Silbert, L.E., Liu, A.J., and S.R. Nagel, Jamming at zero temperature and zero applied stress: The epitome of disorder, Phys. Rev. E, 68, (2003) 40. Otsuki, M., Hayakawa, H., and S. Luding, Behavior of pressure and viscosity at high densities for two-dimensional hard and soft granular materials, Prog. Theor. Phys. Suppl., 184, 110 (2010) 41. Reynolds, O., On the dilatancy of media composed of rigid particles in contact, Phil. Mag. S. 5, 20, (1885) 42. Rudnicki, J.W., and J.R. Rice, Conditions for the localization of deformation in pressure-sensitive dilant materials, J. Mech. Phys. Solids, 23, 371 (1975) 43. Savage, S.B., Analyses of slow high-concentration ows of granular materials, J. Fluid Mech., 377, 1 (1998) 44. Savage, S.B., The mechanics of rapid granular ows, Adv. Appl. Mech., 24, 289 (1984) 45. Sela, N., Goldhirsch, I., and S.N. Noskowicz, Kinetic theoretical study of a simply sheared two-dimensional granular gas to Burnett order, Phys. Fluids, 8, 2337 (1996) 46. Sela, N., and I. Goldhirsch, Hydrodynamic equations for rapid ows of smooth inelastic spheres, to Burnett order, J. Fluid Mech., 361, 41 (1998) 47. Spencer, A.J.M., A theory of the kinematics of ideal soils under plane strain conditions, J. Mech. Phys. Solids, 12, 337 (1964) 48. Vardoulakis, I., and E.C. Aifantis, A gradient ow theory of plasticity for granular materials, Acta Mech., 87, 197 (1991) 49. Wood, D.M., Soil behavior and critical state soil mechanics, Cambridge Univ. Press, (1990) 25
Lecture 6: Flow regimes fluid-like
Granular Flows 1 Lecture 6: Flow regimes fluid-like Quasi-static granular flows have plasticity laws, gaseous granular flows have kinetic theory -- how to model fluid-like flows? Intermediate, dense regime:
More informationExtended kinetic theory applied to dense, granular, simple shear flows
Noname manuscript No. (will be inserted by the editor) Diego Berzi Extended kinetic theory applied to dense, granular, simple shear flows Received: date / Accepted: date Abstract We apply the Extended
More information7 The Navier-Stokes Equations
18.354/12.27 Spring 214 7 The Navier-Stokes Equations In the previous section, we have seen how one can deduce the general structure of hydrodynamic equations from purely macroscopic considerations and
More informationDry granular flows: gas, liquid or solid?
Dry granular flows: gas, liquid or solid? Figure 1: Forterre & Pouliquen, Annu. Rev. Fluid Mechanics, 2008 1 Characterizing size and size distribution Grains are not uniform (size, shape, ) Statistical
More informationContinuum Model of Avalanches in Granular Media
Continuum Model of Avalanches in Granular Media David Chen May 13, 2010 Abstract A continuum description of avalanches in granular systems is presented. The model is based on hydrodynamic equations coupled
More informationSIMULATION OF A 2D GRANULAR COLUMN COLLAPSE ON A RIGID BED
1 SIMULATION OF A 2D GRANULAR COLUMN COLLAPSE ON A RIGID BED WITH LATERAL FRICTIONAL EFFECTS High slope results and comparison with experimental data Nathan Martin1, Ioan Ionescu2, Anne Mangeney1,3 François
More information2 GOVERNING EQUATIONS
2 GOVERNING EQUATIONS 9 2 GOVERNING EQUATIONS For completeness we will take a brief moment to review the governing equations for a turbulent uid. We will present them both in physical space coordinates
More informationSimple shear flow of collisional granular-fluid mixtures
Manuscript Click here to download Manuscript: Manuscript_r1.docx 1 Simple shear flow of collisional granular-fluid mixtures 2 3 4 5 D. Berzi 1 1 Department of Environmental, Hydraulic, Infrastructure,
More informationBifurcation Analysis in Geomechanics
Bifurcation Analysis in Geomechanics I. VARDOULAKIS Department of Engineering Science National Technical University of Athens Greece and J. SULEM Centre d'enseignement et de Recherche en Mecanique des
More informationJoe Goddard, Continuum modeling of granular media
Joe Goddard, jgoddard@ucsd.edu Continuum modeling of granular media This talk summarizes a recent survey [1] of the interesting phenomenology and the prominent régimes of granular flow which also offers
More informationAvailable online at ScienceDirect. Procedia Engineering 103 (2015 )
Available online at www.sciencedirect.com ScienceDirect Procedia Engineering 103 (2015 ) 237 245 The 13 th Hypervelocity Impact Symposium Strength of Granular Materials in Transient and Steady State Rapid
More informationTurbulentlike Quantitative Analysis on Energy Dissipation in Vibrated Granular Media
Copyright 011 Tech Science Press CMES, vol.71, no., pp.149-155, 011 Turbulentlike Quantitative Analysis on Energy Dissipation in Vibrated Granular Media Zhi Yuan Cui 1, Jiu Hui Wu 1 and Di Chen Li 1 Abstract:
More information6 VORTICITY DYNAMICS 41
6 VORTICITY DYNAMICS 41 6 VORTICITY DYNAMICS As mentioned in the introduction, turbulence is rotational and characterized by large uctuations in vorticity. In this section we would like to identify some
More informationEnergy of dislocation networks
Energy of dislocation networks ictor L. Berdichevsky Mechanical Engineering, Wayne State University, Detroit MI 48 USA (Dated: February, 6) Abstract It is obtained an expression for energy of a random
More informationEntropy generation and transport
Chapter 7 Entropy generation and transport 7.1 Convective form of the Gibbs equation In this chapter we will address two questions. 1) How is Gibbs equation related to the energy conservation equation?
More informationAsymptotic solution of the Boltzmann equation for the shear ow of smooth inelastic disks
Physica A 275 (2000) 483 504 www.elsevier.com/locate/physa Asymptotic solution of the Boltzmann equation for the shear ow of smooth inelastic disks V. Kumaran Department of Chemical Engineering, Indian
More informationFundamentals of Fluid Dynamics: Elementary Viscous Flow
Fundamentals of Fluid Dynamics: Elementary Viscous Flow Introductory Course on Multiphysics Modelling TOMASZ G. ZIELIŃSKI bluebox.ippt.pan.pl/ tzielins/ Institute of Fundamental Technological Research
More informationChapter 1 Fluid Characteristics
Chapter 1 Fluid Characteristics 1.1 Introduction 1.1.1 Phases Solid increasing increasing spacing and intermolecular liquid latitude of cohesive Fluid gas (vapor) molecular force plasma motion 1.1.2 Fluidity
More informationGranular materials (Assemblies of particles with dissipation )
Granular materials (Assemblies of particles with dissipation ) Saturn ring Sand mustard seed Ginkaku-ji temple Sheared granular materials packing fraction : Φ Inhomogeneous flow Gas (Φ = 012) Homogeneous
More informationViscoelasticity. Basic Notions & Examples. Formalism for Linear Viscoelasticity. Simple Models & Mechanical Analogies. Non-linear behavior
Viscoelasticity Basic Notions & Examples Formalism for Linear Viscoelasticity Simple Models & Mechanical Analogies Non-linear behavior Viscoelastic Behavior Generic Viscoelasticity: exhibition of both
More information4. The Green Kubo Relations
4. The Green Kubo Relations 4.1 The Langevin Equation In 1828 the botanist Robert Brown observed the motion of pollen grains suspended in a fluid. Although the system was allowed to come to equilibrium,
More informationViscosity of magmas containing highly deformable bubbles
Journal of Volcanology and Geothermal Research 105 (2001) 19±24 www.elsevier.nl/locate/jvolgeores Viscosity of magmas containing highly deformable bubbles M. Manga a, *, M. Loewenberg b a Department of
More informationIndiana University, January T. Witten, University of Chicago
Indiana University, January 2007 T. Witten, University of Chicago Force propagation in a simple solid: two pictures Add circular beads to a container one by one How does an added force reach the ground?
More informationDry and wet granular flows. Diego Berzi
Dry and wet granular flows Diego Berzi Outline 2 What? Why? How? When? Who? Where? Then? What? Granular flows many solid moving particles 3 particle mass is large (at least 10 20 molecular masses). Hence,
More informationMicromechanics of granular materials: slow flows
Micromechanics of granular materials: slow flows Niels P. Kruyt Department of Mechanical Engineering, University of Twente, n.p.kruyt@utwente.nl www.ts.ctw.utwente.nl/kruyt/ 1 Applications of granular
More informationIntroduction to Marine Hydrodynamics
1896 1920 1987 2006 Introduction to Marine Hydrodynamics (NA235) Department of Naval Architecture and Ocean Engineering School of Naval Architecture, Ocean & Civil Engineering First Assignment The first
More informationPEAT SEISMOLOGY Lecture 2: Continuum mechanics
PEAT8002 - SEISMOLOGY Lecture 2: Continuum mechanics Nick Rawlinson Research School of Earth Sciences Australian National University Strain Strain is the formal description of the change in shape of a
More informationChapter 1. Continuum mechanics review. 1.1 Definitions and nomenclature
Chapter 1 Continuum mechanics review We will assume some familiarity with continuum mechanics as discussed in the context of an introductory geodynamics course; a good reference for such problems is Turcotte
More informationGranular Micro-Structure and Avalanche Precursors
Granular Micro-Structure and Avalanche Precursors L. Staron, F. Radjai & J.-P. Vilotte Department of Applied Mathematics and Theoretical Physics, Cambridge CB3 0WA, UK. Laboratoire de Mécanique et Génie
More informationDiscrete element investigation of rate effects on the asymptotic behaviour of granular materials
Discrete element investigation of rate effects on the asymptotic behaviour of granular materials David MAŠÍN a,1 and Jan JERMAN a a Faculty of Science, Charles University in Prague, Czech Republic Abstract.
More informationDilatancy Transition in a Granular Model. David Aristoff and Charles Radin * Mathematics Department, University of Texas, Austin, TX 78712
Dilatancy Transition in a Granular Model by David Aristoff and Charles Radin * Mathematics Department, University of Texas, Austin, TX 78712 Abstract We introduce a model of granular matter and use a stress
More informationSeveral forms of the equations of motion
Chapter 6 Several forms of the equations of motion 6.1 The Navier-Stokes equations Under the assumption of a Newtonian stress-rate-of-strain constitutive equation and a linear, thermally conductive medium,
More informationCHAPTER 7 SEVERAL FORMS OF THE EQUATIONS OF MOTION
CHAPTER 7 SEVERAL FORMS OF THE EQUATIONS OF MOTION 7.1 THE NAVIER-STOKES EQUATIONS Under the assumption of a Newtonian stress-rate-of-strain constitutive equation and a linear, thermally conductive medium,
More information1 Modeling Immiscible Fluid Flow in Porous Media
Excerpts from the Habilitation Thesis of Peter Bastian. For references as well as the full text, see http://cox.iwr.uni-heidelberg.de/people/peter/pdf/bastian_habilitationthesis.pdf. Used with permission.
More informationComputational non-linear structural dynamics and energy-momentum integration schemes
icccbe 2010 Nottingham University Press Proceedings of the International Conference on Computing in Civil and Building Engineering W Tizani (Editor) Computational non-linear structural dynamics and energy-momentum
More informationTIME-DEPENDENT BEHAVIOR OF PILE UNDER LATERAL LOAD USING THE BOUNDING SURFACE MODEL
TIME-DEPENDENT BEHAVIOR OF PILE UNDER LATERAL LOAD USING THE BOUNDING SURFACE MODEL Qassun S. Mohammed Shafiqu and Maarib M. Ahmed Al-Sammaraey Department of Civil Engineering, Nahrain University, Iraq
More informationContents. I Introduction 1. Preface. xiii
Contents Preface xiii I Introduction 1 1 Continuous matter 3 1.1 Molecules................................ 4 1.2 The continuum approximation.................... 6 1.3 Newtonian mechanics.........................
More informationChapter 1 Direct Modeling for Computational Fluid Dynamics
Chapter 1 Direct Modeling for Computational Fluid Dynamics Computational fluid dynamics (CFD) is a scientific discipline, which aims to capture fluid motion in a discretized space. The description of the
More informationNumerical Heat and Mass Transfer
Master Degree in Mechanical Engineering Numerical Heat and Mass Transfer 15-Convective Heat Transfer Fausto Arpino f.arpino@unicas.it Introduction In conduction problems the convection entered the analysis
More informationAnalytical formulation of Modified Upper Bound theorem
CHAPTER 3 Analytical formulation of Modified Upper Bound theorem 3.1 Introduction In the mathematical theory of elasticity, the principles of minimum potential energy and minimum complimentary energy are
More informationL O N G I T U D I N A L V O R T I C E S I N G R A N U L A R F L O W S
L O N G I T U D I N A L V O R T I C E S I N G R A N U L A R F L O W S Yoël FORTERRE, Olivier POULIQUEN Institut Universitaire des Sstèmes Thermiques et Industriels (UMR 6595 CNRS) 5, rue Enrico Fermi 13453
More informationClassical fracture and failure hypotheses
: Chapter 2 Classical fracture and failure hypotheses In this chapter, a brief outline on classical fracture and failure hypotheses for materials under static loading will be given. The word classical
More informationSteady Flow and its Instability of Gravitational Granular Flow
Steady Flow and its Instability of Gravitational Granular Flow Namiko Mitarai Department of Chemistry and Physics of Condensed Matter, Graduate School of Science, Kyushu University, Japan. A thesis submitted
More informationELASTOPLASTICITY THEORY by V. A. Lubarda
ELASTOPLASTICITY THEORY by V. A. Lubarda Contents Preface xiii Part 1. ELEMENTS OF CONTINUUM MECHANICS 1 Chapter 1. TENSOR PRELIMINARIES 3 1.1. Vectors 3 1.2. Second-Order Tensors 4 1.3. Eigenvalues and
More informationReference material Reference books: Y.C. Fung, "Foundations of Solid Mechanics", Prentice Hall R. Hill, "The mathematical theory of plasticity",
Reference material Reference books: Y.C. Fung, "Foundations of Solid Mechanics", Prentice Hall R. Hill, "The mathematical theory of plasticity", Oxford University Press, Oxford. J. Lubliner, "Plasticity
More informationClusters in granular flows : elements of a non-local rheology
CEA-Saclay/SPEC; Group Instabilities and Turbulence Clusters in granular flows : elements of a non-local rheology Olivier Dauchot together with many contributors: D. Bonamy, E. Bertin, S. Deboeuf, B. Andreotti,
More informationMicro-macro modelling for fluids and powders
Micro-macro modelling for fluids and powders Stefan Luding 1,2 1 Particle Technology, DelftChemTech, TU Delft, Julianalaan 136, 2628 BL Delft, The Netherlands 2 e-mail: s.luding@tnw.tudelft.nl ABSTRACT
More informationDifferential criterion of a bubble collapse in viscous liquids
PHYSICAL REVIEW E VOLUME 60, NUMBER 1 JULY 1999 Differential criterion of a bubble collapse in viscous liquids Vladislav A. Bogoyavlenskiy* Low Temperature Physics Department, Moscow State University,
More informationNavier-Stokes Equation: Principle of Conservation of Momentum
Navier-tokes Equation: Principle of Conservation of Momentum R. hankar ubramanian Department of Chemical and Biomolecular Engineering Clarkson University Newton formulated the principle of conservation
More informationBasic concepts in viscous flow
Élisabeth Guazzelli and Jeffrey F. Morris with illustrations by Sylvie Pic Adapted from Chapter 1 of Cambridge Texts in Applied Mathematics 1 The fluid dynamic equations Navier-Stokes equations Dimensionless
More informationTurbulence is a ubiquitous phenomenon in environmental fluid mechanics that dramatically affects flow structure and mixing.
Turbulence is a ubiquitous phenomenon in environmental fluid mechanics that dramatically affects flow structure and mixing. Thus, it is very important to form both a conceptual understanding and a quantitative
More informationA Constitutive Framework for the Numerical Analysis of Organic Soils and Directionally Dependent Materials
Dublin, October 2010 A Constitutive Framework for the Numerical Analysis of Organic Soils and Directionally Dependent Materials FracMan Technology Group Dr Mark Cottrell Presentation Outline Some Physical
More informationChapter 2 Theory. 2.1 Continuum Mechanics of Porous Media Porous Medium Model
Chapter 2 Theory In this chapter we briefly glance at basic concepts of porous medium theory (Sect. 2.1.1) and thermal processes of multiphase media (Sect. 2.1.2). We will study the mathematical description
More informationFrictional rheologies have a wide range of applications in engineering
A liquid-crystal model for friction C. H. A. Cheng, L. H. Kellogg, S. Shkoller, and D. L. Turcotte Departments of Mathematics and Geology, University of California, Davis, CA 95616 ; Contributed by D.
More informationHomogenization in probabilistic terms: the variational principle and some approximate solutions
Homogenization in probabilistic terms: the variational principle and some approximate solutions Victor L. Berdichevsky Mechanical Engineering, Wayne State University, Detroit MI 480 USA (Dated: October
More informationLecture 8: Tissue Mechanics
Computational Biology Group (CoBi), D-BSSE, ETHZ Lecture 8: Tissue Mechanics Prof Dagmar Iber, PhD DPhil MSc Computational Biology 2015/16 7. Mai 2016 2 / 57 Contents 1 Introduction to Elastic Materials
More informationLecture 3: 1. Lecture 3.
Lecture 3: 1 Lecture 3. Lecture 3: 2 Plan for today Summary of the key points of the last lecture. Review of vector and tensor products : the dot product (or inner product ) and the cross product (or vector
More informationn v molecules will pass per unit time through the area from left to
3 iscosity and Heat Conduction in Gas Dynamics Equations of One-Dimensional Gas Flow The dissipative processes - viscosity (internal friction) and heat conduction - are connected with existence of molecular
More informationFluid Mechanics II Viscosity and shear stresses
Fluid Mechanics II Viscosity and shear stresses Shear stresses in a Newtonian fluid A fluid at rest can not resist shearing forces. Under the action of such forces it deforms continuously, however small
More informationMaxwell s equations derived from minimum assumptions
Maxwell s equations derived from minimum assumptions Valery P.Dmitriyev (Dated: December 4, 2011) Maxwell s equations, under disguise of electromagnetic fields occurred in empty space, describe dynamics
More informationBreakdown of Elasticity Theory for Jammed Hard-Particle Packings: Conical Nonlinear Constitutive Theory
Breakdown of Elasticity Theory for Jammed Hard-Particle Packings: Conical Nonlinear Constitutive Theory S. Torquato, 1,2 A. Donev 2,3, and F. H. Stillinger 1 Department of Chemistry, 1 Princeton Materials
More informationSHORT COMMUNICATIONS
INTERNATIONAL JOURNAL FOR NUMERICAL AND ANALYTICAL METHODS IN GEOMECHANICS, VOL. 7, 485492 (ty83) SHORT COMMUNICATIONS ON THE SOLUTION OF PLANE FLOW OF GRANULAR MEDIA FOR JUMP NON-HOMOGENEITY RADOSLAW
More informationLecture #6: 3D Rate-independent Plasticity (cont.) Pressure-dependent plasticity
Lecture #6: 3D Rate-independent Plasticity (cont.) Pressure-dependent plasticity by Borja Erice and Dirk Mohr ETH Zurich, Department of Mechanical and Process Engineering, Chair of Computational Modeling
More informationRheology of granular flows: Role of the interstitial fluid
Rheology of granular flows: Role of the interstitial fluid Colorado 2003, USGS Olivier Pouliquen, IUSTI, CNRS, Aix-Marseille University Marseille, France Motivations : debris flows, landslides, avalanches,
More informationFluid Mechanics Prof. T.I. Eldho Department of Civil Engineering Indian Institute of Technology, Bombay. Lecture - 17 Laminar and Turbulent flows
Fluid Mechanics Prof. T.I. Eldho Department of Civil Engineering Indian Institute of Technology, Bombay Lecture - 17 Laminar and Turbulent flows Welcome back to the video course on fluid mechanics. In
More informationAnisotropic grid-based formulas. for subgrid-scale models. By G.-H. Cottet 1 AND A. A. Wray
Center for Turbulence Research Annual Research Briefs 1997 113 Anisotropic grid-based formulas for subgrid-scale models By G.-H. Cottet 1 AND A. A. Wray 1. Motivations and objectives Anisotropic subgrid-scale
More informationISSUES IN MATHEMATICAL MODELING OF STATIC AND DYNAMIC LIQUEFACTION AS A NON-LOCAL INSTABILITY PROBLEM. Ronaldo I. Borja Stanford University ABSTRACT
ISSUES IN MATHEMATICAL MODELING OF STATIC AND DYNAMIC LIQUEFACTION AS A NON-LOCAL INSTABILITY PROBLEM Ronaldo I. Borja Stanford University ABSTRACT The stress-strain behavior of a saturated loose sand
More informationTable of Contents. Preface... xiii
Preface... xiii PART I. ELEMENTS IN FLUID MECHANICS... 1 Chapter 1. Local Equations of Fluid Mechanics... 3 1.1. Forces, stress tensor, and pressure... 4 1.2. Navier Stokes equations in Cartesian coordinates...
More informationModelling the excavation damaged zone in Callovo-Oxfordian claystone with strain localisation
Modelling the excavation damaged zone in Callovo-Oxfordian claystone with strain localisation B. Pardoen - F. Collin - S. Levasseur - R. Charlier Université de Liège ArGEnCo ALERT Workshop 2012 Aussois,
More informationMolecular dynamics simulations of sliding friction in a dense granular material
Modelling Simul. Mater. Sci. Eng. 6 (998) 7 77. Printed in the UK PII: S965-393(98)9635- Molecular dynamics simulations of sliding friction in a dense granular material T Matthey and J P Hansen Department
More informationCrack dynamics in elastic media
PHILOSOPHICAL MAGAZINE B, 1998, VOL. 78, NO. 2, 97± 102 Crack dynamics in elastic media By Mokhtar Adda-Bedia and Martine Ben Amar Laboratoire de Physique Statistique de l Ecole Normale Supe  rieure,
More informationViscous Fluids. Amanda Meier. December 14th, 2011
Viscous Fluids Amanda Meier December 14th, 2011 Abstract Fluids are represented by continuous media described by mass density, velocity and pressure. An Eulerian description of uids focuses on the transport
More informationCHAPTER 8 ENTROPY GENERATION AND TRANSPORT
CHAPTER 8 ENTROPY GENERATION AND TRANSPORT 8.1 CONVECTIVE FORM OF THE GIBBS EQUATION In this chapter we will address two questions. 1) How is Gibbs equation related to the energy conservation equation?
More information2 D.D. Joseph To make things simple, consider flow in two dimensions over a body obeying the equations ρ ρ v = 0;
Accepted for publication in J. Fluid Mech. 1 Viscous Potential Flow By D.D. Joseph Department of Aerospace Engineering and Mechanics, University of Minnesota, MN 55455 USA Email: joseph@aem.umn.edu (Received
More informationDETERMINATION OF UPPER BOUND LIMIT ANALYSIS OF THE COEFFICIENT OF LATERAL PASSIVE EARTH PRESSURE IN THE CONDITION OF LINEAR MC CRITERIA
DETERMINATION OF UPPER BOUND LIMIT ANALYSIS OF THE COEFFICIENT OF LATERAL PASSIVE EARTH PRESSURE IN THE CONDITION OF LINEAR MC CRITERIA Ghasemloy Takantapeh Sasan, *Akhlaghi Tohid and Bahadori Hadi Department
More informationCRACK-TIP DRIVING FORCE The model evaluates the eect of inhomogeneities by nding the dierence between the J-integral on two contours - one close to th
ICF 100244OR Inhomogeneity eects on crack growth N. K. Simha 1,F.D.Fischer 2 &O.Kolednik 3 1 Department ofmechanical Engineering, University of Miami, P.O. Box 248294, Coral Gables, FL 33124-0624, USA
More informationFE-studies of a Deterministic and Statistical Size Effect in Granular Bodies Including Shear Localization
The 1 th International Conference of International Association for Computer Methods and Advances in Geomechanics (IACMAG) 1- October, Goa, India FE-studies of a Deterministic and Statistical Size Effect
More informationGame Physics. Game and Media Technology Master Program - Utrecht University. Dr. Nicolas Pronost
Game and Media Technology Master Program - Utrecht University Dr. Nicolas Pronost Soft body physics Soft bodies In reality, objects are not purely rigid for some it is a good approximation but if you hit
More informationUniversality of shear-banding instability and crystallization in sheared granular fluid
Under consideration for publication in J. Fluid Mech. 1 Universality of shear-banding instability and crystallization in sheared granular fluid MEEBOOB ALAM 1, PRIYANKA SUKLA 1 AND STEFAN LUDING 2 1 Engineering
More informationStress and fabric in granular material
THEORETICAL & APPLIED MECHANICS LETTERS 3, 22 (23) Stress and fabric in granular material Ching S. Chang,, a) and Yang Liu 2 ) Department of Civil Engineering, University of Massachusetts Amherst, Massachusetts
More informationMicro-Macro transition (from particles to continuum theory) Granular Materials. Approach philosophy. Model Granular Materials
Micro-Macro transition (from particles to continuum theory) Stefan Luding MSM, TS, CTW, UTwente, NL Stefan Luding, s.luding@utwente.nl MSM, TS, CTW, UTwente, NL Granular Materials Real: sand, soil, rock,
More informationSOIL MECHANICS AND PLASTIC ANALYSIS OR LIMIT DESIGN*
157 SOIL MECHANICS AND PLASTIC ANALYSIS OR LIMIT DESIGN* BY D. C. DRUCKER and W. PRAGER Brown University 1. Introduction. Problems of soil mechanics involving stability of slopes, bearing capacity of foundation
More informationMeasurements of the yield stress in frictionless granular systems
Measurements of the yield stress in frictionless granular systems Ning Xu 1 and Corey S. O Hern 1,2 1 Department of Mechanical Engineering, Yale University, New Haven, Connecticut 06520-8284, USA 2 Department
More informationReview of Fluid Mechanics
Chapter 3 Review of Fluid Mechanics 3.1 Units and Basic Definitions Newton s Second law forms the basis of all units of measurement. For a particle of mass m subjected to a resultant force F the law may
More informationChapter 9: Differential Analysis of Fluid Flow
of Fluid Flow Objectives 1. Understand how the differential equations of mass and momentum conservation are derived. 2. Calculate the stream function and pressure field, and plot streamlines for a known
More informationDiscrete element modeling of self-healing processes in damaged particulate materials
Discrete element modeling of self-healing processes in damaged particulate materials S. Luding 1, A.S.J. Suiker 2, and I. Kadashevich 1 1) Particle Technology, Nanostructured Materials, DelftChemTech,
More informationMicrostructural Randomness and Scaling in Mechanics of Materials. Martin Ostoja-Starzewski. University of Illinois at Urbana-Champaign
Microstructural Randomness and Scaling in Mechanics of Materials Martin Ostoja-Starzewski University of Illinois at Urbana-Champaign Contents Preface ix 1. Randomness versus determinism ix 2. Randomness
More informationINDEX 363. Cartesian coordinates 19,20,42, 67, 83 Cartesian tensors 84, 87, 226
INDEX 363 A Absolute differentiation 120 Absolute scalar field 43 Absolute tensor 45,46,47,48 Acceleration 121, 190, 192 Action integral 198 Addition of systems 6, 51 Addition of tensors 6, 51 Adherence
More informationOn Phase Transition and Self-Organized Critical State in Granular Packings
arxiv:cond-mat/9812204v1 [cond-mat.dis-nn] 11 Dec 1998 On Phase Transition and Self-Organized Critical State in Granular Packings Einat Aharonov 1, David Sparks 2, 1 Lamont-Doherty Earth-Observatory, Columbia
More informationV (r,t) = i ˆ u( x, y,z,t) + ˆ j v( x, y,z,t) + k ˆ w( x, y, z,t)
IV. DIFFERENTIAL RELATIONS FOR A FLUID PARTICLE This chapter presents the development and application of the basic differential equations of fluid motion. Simplifications in the general equations and common
More informationContinuum Mechanics. Continuum Mechanics and Constitutive Equations
Continuum Mechanics Continuum Mechanics and Constitutive Equations Continuum mechanics pertains to the description of mechanical behavior of materials under the assumption that the material is a uniform
More informationKINEMATICS OF CONTINUA
KINEMATICS OF CONTINUA Introduction Deformation of a continuum Configurations of a continuum Deformation mapping Descriptions of motion Material time derivative Velocity and acceleration Transformation
More informationDisplacement charts for slopes subjected to seismic loads
Computers and Geotechnics 25 (1999) 45±55 www.elsevier.com/locate/compgeo Technical Note Displacement charts for slopes subjected to seismic loads Liangzhi You a, Radoslaw L. Michalowski a,b, * a Department
More informationSchiestel s Derivation of the Epsilon Equation and Two Equation Modeling of Rotating Turbulence
NASA/CR-21-2116 ICASE Report No. 21-24 Schiestel s Derivation of the Epsilon Equation and Two Equation Modeling of Rotating Turbulence Robert Rubinstein NASA Langley Research Center, Hampton, Virginia
More informationLaminar Forced Convection Heat Transfer from Two Heated Square Cylinders in a Bingham Plastic Fluid
Laminar Forced Convection Heat Transfer from Two Heated Square Cylinders in a Bingham Plastic Fluid E. Tejaswini 1*, B. Sreenivasulu 2, B. Srinivas 3 1,2,3 Gayatri Vidya Parishad College of Engineering
More informationCritical scaling near the yielding transition in granular media
Critical scaling near the yielding transition in granular media Abram H. Clark, 1 Mark D. Shattuck, 2 Nicholas T. Ouellette, 3 1, 4, 5 and Corey S. O Hern 1 Department of Mechanical Engineering and Materials
More informationElements of Rock Mechanics
Elements of Rock Mechanics Stress and strain Creep Constitutive equation Hooke's law Empirical relations Effects of porosity and fluids Anelasticity and viscoelasticity Reading: Shearer, 3 Stress Consider
More informationTWO-DIMENSIONAL MAGMA FLOW *
Iranian Journal of Science & Technology, Transaction A, Vol. 34, No. A2 Printed in the Islamic Republic of Iran, 2010 Shiraz University TWO-DIMENSIONAL MAGMA FLOW * A. MEHMOOD 1** AND A. ALI 2 1 Department
More informationMath 575-Lecture Viscous Newtonian fluid and the Navier-Stokes equations
Math 575-Lecture 13 In 1845, tokes extended Newton s original idea to find a constitutive law which relates the Cauchy stress tensor to the velocity gradient, and then derived a system of equations. The
More informationThis false color image is taken from Dan Howell's experiments. This is a 2D experiment in which a collection of disks undergoes steady shearing.
This false color image is taken from Dan Howell's experiments. This is a 2D experiment in which a collection of disks undergoes steady shearing. The red regions mean large local force, and the blue regions
More information