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A distributed Lagrange multiplier/fictitious domain method for viscoelastic particulate flows

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TLDR
In this paper, a distributed Lagrange multiplier/fictitious domain method (DLM) is developed for simulating the motion of rigid particles suspended in the Oldroyd-B fluid.
Abstract
A distributed Lagrange multiplier/fictitious domain method (DLM) is developed for simulating the motion of rigid particles suspended in the Oldroyd-B fluid. This method is a generalization of the one described in [R. Glowinski, T.W. Pan, T.I. Hesla, D.D. Joseph, Int. J. Multiphase Flows 25 (1998) 755–794] where the motion of particles suspended in a Newtonian fluid was simulated. In our implementation of the DLM method, the fluid–particle system is treated implicitly using a combined weak formulation in which the forces and moments between the particles and fluid cancel. The governing equations for the Oldroyd-B liquid are solved everywhere, including inside the particles. The flow inside the particles is forced to be a rigid body motion by a distribution of Lagrange multipliers. We use the Marchuk–Yanenko operator-splitting technique to decouple the difficulties associated with the incompressibility constraint, nonlinear convection and viscoelastic terms. The constitutive equation is solved using a scheme that guarantees the positive definiteness of the configuration tensor, while the convection term in the constitutive equation is discretized using a third-order upwinding scheme. The nonlinear convection problem is solved using a least square conjugate gradient algorithm, and the Stokes-like problem is solved using a conjugate gradient algorithm. The code is verified performing a convergence study to show that the results are independent of the mesh and time step sizes. Our simulations show that, when particles are dropped in a channel, and the viscoelastic Mach number (M) is less than 1 and the elasticity number (E) is greater than 1, the particles chain along the flow direction; this agrees with the results presented in [P.Y. Huang, H.H. Hu, D.D. Joseph, J. Fluid Mech. 362 (1998) 297–325]. In our simulations of the fluidization of 102 particles in a two-dimensional bed, we find that the particles near the channel walls form chains that are parallel to the walls, but the distribution of particles away from the walls is relatively random.

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Citations
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Discrete particle simulation of particulate systems: Theoretical developments

TL;DR: This paper reviews the work in this area with special reference to the discrete element method and associated theoretical developments, and covers three important aspects: models for the calculation of the particle–particle and particle–fluid interaction forces, coupling of discrete elements method with computational fluid dynamics to describe particle-fluid flow, and the theories for linking discrete to continuum modelling.
Journal ArticleDOI

Direct numerical simulations of fluid-solid systems using the arbitrary Langrangian-Eulerian technique

TL;DR: This paper presents the most up-to-date implementation of the method and the results of several benchmark test problems for direct simulations of fluid–solid systems using the arbitrary Lagrangian–Eulerian technique.
Journal ArticleDOI

A new formulation of the distributed Lagrange multiplier/fictitious domain method for particulate flows

TL;DR: In this article, a Lagrange-multiplier-based fictitious-domain method (DLM) for the direct numerical simulation of rigid particulate flows in a Newtonian fluid was presented, where the flow in the particle domain is constrained to be a rigid body motion by using a well-chosen field of Lagrange multipliers.
Journal ArticleDOI

Particle-scale modelling of gas-solid flow in fluidisation †

TL;DR: The applicability of CCDM is highlighted by its successful simulation of complicated phenomena associated with the transition between fluid-like and solid-like behaviour in raceway formation and bed expansion, and the usefulness of the resulting particle-scale information is demonstrated in elucidating the fundamentals governing the gas-solid flow.
References
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Book

Numerical heat transfer and fluid flow

TL;DR: In this article, the authors focus on heat and mass transfer, fluid flow, chemical reaction, and other related processes that occur in engineering equipment, the natural environment, and living organisms.
Journal ArticleDOI

Numerical Heat Transfer and Fluid Flow

TL;DR: In this paper, numerical heat transfer and fluid flow are used to transfer heat from a nuclear power plant to a nuclear fluid flow system, and the resulting fluid flow is used for nuclear power plants.
Journal ArticleDOI

A distributed Lagrange multiplier/fictitious domain method for particulate flows

TL;DR: In this article, a new Lagrange-multiplier based fictitious-domain method is presented for the direct numerical simulation of viscous incompressible flow with suspended solid particles, which uses a finite-element discretization in space and an operator-splitting technique for discretisation in time.
Book

Fluid dynamics of viscoelastic liquids

TL;DR: In this article, a mathematical and physical theory which takes a proper account of the elasticity of liquids is developed, which leads to systems of partial differential equations of composite type in which some variables are hyperbolic and others elliptic.
Journal ArticleDOI

Direct simulation of flows of solid-liquid mixtures

TL;DR: In this paper, a generalized Galerkin finite element formulation was developed to simulate the motion of a large number of solid particles in a flowing liquid, where the nodes in the interior of the fluid were computed using Laplace's equation to guarantee a smoothly varying distribution of the nodes.
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