Antisymmetric Stress Tensor
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AST242 LECTURE NOTES PART 3 Contents 1. Viscous Flows 2 1.1. the Velocity Gradient Tensor 2 1.2. Viscous Stress Tensor 3 1.3. Na
AST242 LECTURE NOTES PART 3 Contents 1. Viscous flows 2 1.1. The velocity gradient tensor 2 1.2. Viscous stress tensor 3 1.3. Navier Stokes equation { diffusion 5 1.4. Viscosity to order of magnitude 6 1.5. Example using the viscous stress tensor: The force on a moving plate 6 1.6. Example using the Navier Stokes equation { Poiseuille flow or Flow in a capillary 7 1.7. Viscous Energy Dissipation 8 2. The Accretion disk 10 2.1. Accretion to order of magnitude 14 2.2. Hydrostatic equilibrium for an accretion disk 15 2.3. Shakura and Sunyaev's α-disk 17 2.4. Reynolds Number 17 2.5. Circumstellar disk heated by stellar radiation 18 2.6. Viscous Energy Dissipation 20 2.7. Accretion Luminosity 21 3. Vorticity and Rotation 24 3.1. Helmholtz Equation 25 3.2. Rate of Change of a vector element that is moving with the fluid 26 3.3. Kelvin Circulation Theorem 28 3.4. Vortex lines and vortex tubes 30 3.5. Vortex stretching and angular momentum 32 3.6. Bernoulli's constant in a wake 33 3.7. Diffusion of vorticity 34 3.8. Potential Flow and d'Alembert's paradox 34 3.9. Burger's vortex 36 4. Rotating Flows 38 4.1. Coriolis Force 38 4.2. Rossby and Ekman numbers 39 4.3. Geostrophic flows and the Taylor Proudman theorem 39 4.4. Two dimensional flows on the surface of a planet 41 1 2 AST242 LECTURE NOTES PART 3 4.5. Thermal winds? 42 5. -
Lecture 1: Introduction
Lecture 1: Introduction E. J. Hinch Non-Newtonian fluids occur commonly in our world. These fluids, such as toothpaste, saliva, oils, mud and lava, exhibit a number of behaviors that are different from Newtonian fluids and have a number of additional material properties. In general, these differences arise because the fluid has a microstructure that influences the flow. In section 2, we will present a collection of some of the interesting phenomena arising from flow nonlinearities, the inhibition of stretching, elastic effects and normal stresses. In section 3 we will discuss a variety of devices for measuring material properties, a process known as rheometry. 1 Fluid Mechanical Preliminaries The equations of motion for an incompressible fluid of unit density are (for details and derivation see any text on fluid mechanics, e.g. [1]) @u + (u · r) u = r · S + F (1) @t r · u = 0 (2) where u is the velocity, S is the total stress tensor and F are the body forces. It is customary to divide the total stress into an isotropic part and a deviatoric part as in S = −pI + σ (3) where tr σ = 0. These equations are closed only if we can relate the deviatoric stress to the velocity field (the pressure field satisfies the incompressibility condition). It is common to look for local models where the stress depends only on the local gradients of the flow: σ = σ (E) where E is the rate of strain tensor 1 E = ru + ruT ; (4) 2 the symmetric part of the the velocity gradient tensor. The trace-free requirement on σ and the physical requirement of symmetry σ = σT means that there are only 5 independent components of the deviatoric stress: 3 shear stresses (the off-diagonal elements) and 2 normal stress differences (the diagonal elements constrained to sum to 0). -
CONTINUUM MECHANICS for ENGINEERS Second Edition Second Edition
CONTINUUM MECHANICS for ENGINEERS Second Edition Second Edition CONTINUUM MECHANICS for ENGINEERS G. Thomas Mase George E. Mase CRC Press Boca Raton London New York Washington, D.C. Library of Congress Cataloging-in-Publication Data Mase, George Thomas. Continuum mechanics for engineers / G. T. Mase and G. E. Mase. -- 2nd ed. p. cm. Includes bibliographical references (p. )and index. ISBN 0-8493-1855-6 (alk. paper) 1. Continuum mechanics. I. Mase, George E. QA808.2.M364 1999 531—dc21 99-14604 CIP This book contains information obtained from authentic and highly regarded sources. Reprinted material is quoted with permission, and sources are indicated. A wide variety of references are listed. Reasonable efforts have been made to publish reliable data and informa- tion, but the author and the publisher cannot assume responsibility for the validity of all materials or for the consequences of their use. Neither this book nor any part may be reproduced or transmitted in any form or by any means, electronic or mechanical, including photocopying, microfilming, and recording, or by any information storage or retrieval system, without prior permission in writing from the publisher. The consent of CRC Press LLC does not extend to copying for general distribution, for promotion, for creating new works, or for resale. Specific permission must be obtained in writing from CRC Press LLC for such copying. Direct all inquiries to CRC Press LLC, 2000 N.W. Corporate Blvd., Boca Raton, Florida 33431. Trademark Notice: Product or corporate names may be trademarks or registered trademarks, and are only used for identification and explanation, without intent to infringe. -
C:\Book\Booktex\Notind.Dvi 0
362 INDEX A Cauchy stress law 216 Absolute differentiation 120 Cauchy-Riemann equations 293,321 Absolute scalar field 43 Charge density 323 Absolute tensor 45,46,47,48 Christoffel symbols 108,110,111 Acceleration 121, 190, 192 Circulation 293 Action integral 198 Codazzi equations 139 Addition of systems 6, 51 Coefficient of viscosity 285 Addition of tensors 6, 51 Cofactors 25, 26, 32 Adherence boundary condition 294 Compatibility equations 259, 260, 262 Aelotropic material 245 Completely skew symmetric system 31 Affine transformation 86, 107 Compound pendulum 195,209 Airy stress function 264 Compressible material 231 Almansi strain tensor 229 Conic sections 151 Alternating tensor 6,7 Conical coordinates 74 Ampere’s law 176,301,337,341 Conjugate dyad 49 Angle between vectors 80, 82 Conjugate metric tensor 36, 77 Angular momentum 218, 287 Conservation of angular momentum 218, 295 Angular velocity 86,87,201,203 Conservation of energy 295 Arc length 60, 67, 133 Conservation of linear momentum 217, 295 Associated tensors 79 Conservation of mass 233, 295 Auxiliary Magnetic field 338 Conservative system 191, 298 Axis of symmetry 247 Conservative electric field 323 B Constitutive equations 242, 251,281, 287 Continuity equation 106,234, 287, 335 Basic equations elasticity 236, 253, 270 Contraction 6, 52 Basic equations for a continuum 236 Contravariant components 36, 44 Basic equations of fluids 281, 287 Contravariant tensor 45 Basis vectors 1,2,37,48 Coordinate curves 37, 67 Beltrami 262 Coordinate surfaces 37, 67 Bernoulli’s Theorem 292 Coordinate transformations -
Downstream Instability of Viscoelastic Flow Past a Cylinder
Proceeding of the 12-th ASAT Conference, 29-31 May 2007 CFD-02 1 12-th International Conference Military Technical College on Kobry El-Kobba Aerospace Sciences & Cairo, Egypt Aviation Technology DOWNSTREAM INSTABILITY OF VISCOELASTIC FLOW PAST A CYLINDER H. KAMAL§*, H. NAJI*, L. THAIS* & G. MOMPEAN* ABSTRACT This work aims at simulating two-dimensional viscoelastic incompressible fluid flow past a non-confined cylinder. The finite volume method is used to descritize the governing equations written in the generalized orthogonal coordinate system. For the viscoelastic constitutive equation, two models are studied; the Oldryod-B model and the Phan-Thien-Tanner model PTT model. The quadratic scheme QUICK is employed to evaluate the convection terms. The terms of diffusion, advection and acceleration are treated explicitly. The Elastic Viscous Split Stresses (EVSS) scheme is used to decompose the stress tensor to enhance the stability of computations. The obtained results indicate that, for Newtonian flow, the onset of von Karman street occurs at Reynolds number Re ≥ 47. Upon the onset of vortex shedding the downstream instability zone is elongated and the shedding frequency is reduced. The PTT model proves more stability of computations and reached higher Deborah numbers. KEY WORDS Viscoelastic Fluids, Generalized Orthogonal Coordinates, Flow past a Cylinder § Egyptian Armed Forces * Laboratoire de Mécanique de Lille, UMR-CNRS 8107 Université des Sciences et Technologies de Lille, Polytech’Lille - Cité Scientifique, 59655 Villeneuve d’Ascq Cedex, France [email protected] Proceeding of the 12-th ASAT Conference, 29-31 May 2007 CFD-02 2 NOMENCLATURE Latin symbols: A cylinder radius. aˆ i covariant base vectors . -
Viscoelastic Analogy for the Acceleration and Collimation of Astrophysical Jets
View metadata, citation and similar papers at core.ac.uk brought to you by CORE provided by CERN Document Server Viscoelastic Analogy for the Acceleration and Collimation of Astrophysical Jets Peter T. Williams Department of Physics, University of Florida, Gainesville, FL 32611 1 ABSTRACT Jets are ubiquitous in astronomy. It has been conjectured that the existence of jets is intimately connected with the spin of the central object and the viscous an- gular momentum transport of the inner disk. Bipolar jet-like structures propelled by the viscous torque on a spinning central object are also known in a completely different context, namely the flow in the laboratory of a viscoelastic fluid. On the basis of an analogy of the tangled magnetic field lines of magnetohydrodynamic (MHD) turbulence to the tangled polymers of viscoelastic polymer solutions, we propose a viscoelastic description of the dynamics of highly turbulent conductive fluid. We argue that the same mechanism that forms jets in viscoelastic fluids in the laboratory may be responsible for collimating and powering astrophysical jets by the angular momentum of the central object. Subject headings: MHD — turbulence — stars: winds, outflows — galaxies: jets 1. Introduction Viscoelastic behavior is characteristic of fluids such as polymer suspensions in which long molecular chains become entangled. The deformation and disruption of this entanglement that occurs when the fluid is subjected to shear, and the relaxation to a new entangled state, give such fluids a “memory” that ordinary Newtonian fluids do not have. Egg whites are one common household example. These fluids are in a sense midway between being elastic solids and Newtonian fluids, being more one or the other depending upon the ratio of the relaxation time of the entangled polymers to the deformation time scale. -
III.3.3 Newtonian Fluid: Navier–Stokes Equation
34 Fundamental equations of non-relativistic fluid dynamics III.3.3 Newtonian fluid: Navier–Stokes equation In a real moving fluid, there are friction forces that contribute to the transport of momentum between neighboring fluid layers when the latter are in relative motion. Accordingly, the momentum flux-density tensor is no longer given by Eq. (III.21b) or (III.22), but now contains extra terms, involving derivatives of the flow velocity. Accordingly, the Euler equation must be replaced by an alternative dynamical equation, including the friction forces. :::::::III.3.3 a::::::::::::::::::::::::::::::::::::::::::::::Momentum flux density in a Newtonian fluid The momentum flux density (III.21b) in a perfect fluid only contains two terms—one propor- tional to the components gij of the inverse metric tensor, the other proportional to vi(t;~r) vj(t;~r). Since the coefficients in front of these two terms could a priori depend on~v2, this represents the most general symmetric tensor of degree 2 which can be constructed with the help of the flow velocity only. If the use of terms that depend on the spatial derivatives of the velocity field is also allowed, the components of the momentum flux-density tensor can be of the following form, where for the sake of brevity the variables t and ~r are omitted ! @vi @vj @2v Tij = Pgij + ρvi vj + A + B + O i + ··· ; (III.25) @xj @xi @xj @xk with A, B coefficients that depend on i, j and on the fluid under consideration. As discussed in Sec. I.1.3, the description of a system of particles as a continuous medium, and in particular as a fluid, in local thermodynamic equilibrium, rests on the assumption that the macroscopic quantities of relevance for the medium vary slowly both in space and time. -
Information to Users
INFORMATION TO USERS This manuscript has been reproduced from the microfilm master. UMI films the text directly from the original or copy submitted. Thus, some thesis and dissertation copies are in typewriter face, while others may be from any type of computer printer. The quality of this reproduction is dependent upon the quality of the copy submitted. Broken or indistinct print, colored or poor quality illustrations and photographs, print bleedthrougb, substandard margins, and improper alignment can adversely afreet reproduction. In the unlikely event that the author did not send UMI a complete manuscript and there are missing pages, these will be noted. Also, if unauthorized copyright material had to be removed, a note will indicate the deletion. • Oversize materials (e.g., maps, drawings, charts) are reproduced by sectioning the original, beginning at the upper left-hand comer and continuing from left to right in equal sections with small overlaps. Each original is also photographed in one exposure and is included in reduced form at the back of the book. Photographs included in the original manuscript have been reproduced xerographically in this copy. Higher quality 6" x 9" black and white photographic prints are available for any photographs or illustrations appearing in this copy for an additional charge. Contact UMI directly to order. A Bell & Howell Information Company 300 North Z e e b Road. Ann Arbor. Ml 48106-1346 USA 313/761-4700 800/521-0600 ANALYSIS OF MORPHOLOGY, CRYSTALLIZATION KINETICS, AND PROPERTIES OF HEAT AFFECTED ZONE IN HOT PLATE WELDING OF POLYPROPYLENE DISSERTATION Presented in Partial Fulfillment of the Requirements for the Degree of Philosophy in the Graduate School of The Ohio State University By Jenn-Yeu Nieh, B.S., M.S. -
1 Collision of Viscoelastic Particles with Adhesion 1.1 Introduction
1 Collision of viscoelastic particles with adhesion ¢¡ £ Nikolai V. Brilliantov 1 and Thorsten Posc¨ hel Department of Physics, Moscow State University, 119899 Vorobievy Gory, Moscow, Russia £ Institut fur¨ Biochemie, Charite,´ Monbijoustraße 2, 10117 Berlin, Germany Abstract: The collision of convex bodies is considered for small impact velocity, when plastic deformation and fragmentation may be disregarded. In this regime the contact is governed by forces according to viscoelastic deformation and by adhesion. The viscoelastic interaction is described by a modified Hertz law while for the adhesive interactions the model by Johnson, Kendall and Roberts (JKR) is adopted. We solve the general contact problem of convex vis- coelastic bodies in quasistatic approximation, which implies that the impact velocity is much smaller than the speed of sound in the material and that the viscosity relaxation time is much smaller than the duration of a collision. We estimate the threshold impact velocity which dis- criminates restitutive and sticking collisions. If the impact velocity is not large as compared with the thresold velocity, adhesive interaction becomes important, thus limiting the validity of the pure viscoelastic collision model. 1.1 Introduction The large set of phenomena observed in granular systems, ranging from sand and powders on Earth to granular gases in planetary rings and protoplanetary discs, is caused by the specific particle interaction. Besides elastic forces, common for molecular or atomic materials (solids, liquids and gases), colliding granular particles exert also dissipative forces. These forces correspond to the dissipation of mechanical energy in the bulk of the grain material as well as on their surfaces. The dissipated energy transforms into energy of the internal degrees of freedom of the grains, that is, the particles are heated. -
A Basic Introduction to Rheology
WHITEPAPER A Basic Introduction to Rheology RHEOLOGY AND Introduction VISCOSITY Rheometry refers to the experimental technique used to determine the rheological properties of materials; rheology being defined as the study of the flow and deformation of matter which describes the interrelation between force, deformation and time. The term rheology originates from the Greek words ‘rheo’ translating as ‘flow’ and ‘logia’ meaning ‘the study of’, although as from the definition above, rheology is as much about the deformation of solid-like materials as it is about the flow of liquid-like materials and in particular deals with the behavior of complex viscoelastic materials that show properties of both solids and liquids in response to force, deformation and time. There are a number of rheometric tests that can be performed on a rheometer to determine flow properties and viscoelastic properties of a material and it is often useful to deal with them separately. Hence for the first part of this introduction the focus will be on flow and viscosity and the tests that can be used to measure and describe the flow behavior of both simple and complex fluids. In the second part deformation and viscoelasticity will be discussed. Viscosity There are two basic types of flow, these being shear flow and extensional flow. In shear flow fluid components shear past one another while in extensional flow fluid component flowing away or towards from one other. The most common flow behavior and one that is most easily measured on a rotational rheometer or viscometer is shear flow and this viscosity introduction will focus on this behavior and how to measure it. -
A Constitutive Framework for the Non-Newtonian Pressure Tensor of a Simple fluid Under Planar flows
A constitutive framework for the non-Newtonian pressure tensor of a simple fluid under planar flows Remco Hartkamp∗ and Stefan Ludingy Multi Scale Mechanics, Faculty of Engineering Technology, MESA+ Institute for Nanotechnology, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands B. D. Toddz Mathematics Discipline, Faculty of Engineering and Industrial Sciences and Centre for Molecular Simulation, Swinburne University of Technology, Hawthorn, Victoria 3122, Australia (Dated: May 24, 2013) Non-equilibrium molecular dynamics simulations of an atomic fluid under shear flow, pla- nar elongational flow and a combination of shear and elongational flow are unified consis- tently with a tensorial model over a wide range of strain rates. A model is presented that predicts the pressure tensor for a non-Newtonian bulk fluid under a homogeneous planar flow field. The model provides a quantitative description of the strain-thinning viscosity, pressure dilatancy, deviatoric viscoelastic lagging and out-of-flow-plane pressure anisotropy. The non-equilibrium pressure tensor is completely described through these four quantities and can be calculated as a function of the equilibrium material constants and the velocity gradient. This constitutive framework in terms of invariants of the pressure tensor departs from the conventional description that deals with an orientation-dependent description of shear stresses and normal stresses. The present model makes it possible to predict the full pressure tensor for a simple fluid under various types of flow without having to produce these flow types explicitly in a simulation or experiment. I. INTRODUCTION There is significant scientific and industrial interest in describing the relation between the pres- sure tensor for non-Newtonian fluids out of thermodynamic equilibrium and other quantities, such as the strain rate and the fluid density and temperature. -
1 the Navier–Stokes Equations
1 The Navier–Stokes Equations Remark 1.1. Basic principles and variables. The basic equations of fluid dy- namics are called Navier–Stokes equations. In the case of an isothermal flow, a flow at constant temperature, they represent two physical conservation laws – the conservation of mass and the conservation of linear momentum. There are various ways for deriving these equations. Here, the classical one of continuum mechanics will be used. Let the flow variables be • ρ(t, x) : density [kg/m3], • v(t, x) : velocity [m/s], • P (t, x) : pressure [N/m2], which are assumed to be sufficiently smooth functions in the time interval [0, T ] and the domain Ω ⊂ R3. 2 Fig. 1.1. Left: Claude Louis Marie Henri Navier (1785 – 1836), right: George Gabriel Stokes (1819 – 1903). 4 1 The Navier–Stokes Equations 1.1 The Conservation of Mass Remark 1.2. General conservation law. Let V be an arbitrary open volume in Ω with sufficiently smooth surface ∂V which is constant in time and with mass m(t) = ρ(t, x) dx, [kg]. ZV If mass in V is conserved, the rate of change of mass in V must be equal to the flux of mass ρv(t, x) [kg/(m2s)] across the boundary ∂V of V d d m(t) = ρ(t, x) dx = − (ρv)(t, s) · n(s) ds, (1.1) dt dt ZV Z∂V where n(s) is the outward pointing unit normal on s ∈ ∂V . Since all functions are assumed to be sufficiently smooth, the divergence theorem can be applied (integration by parts), which gives ∇ · (ρv)(t, x) dx = (ρv)(t, s) · n(s) ds.