Numerical Analysis and Fluid Flow Modeling of Incompressible Navier-Stokes Equations
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An Introduction to Fluid Mechanics: Supplemental Web Appendices
An Introduction to Fluid Mechanics: Supplemental Web Appendices Faith A. Morrison Professor of Chemical Engineering Michigan Technological University November 5, 2013 2 c 2013 Faith A. Morrison, all rights reserved. Appendix C Supplemental Mathematics Appendix C.1 Multidimensional Derivatives In section 1.3.1.1 we reviewed the basics of the derivative of single-variable functions. The same concepts may be applied to multivariable functions, leading to the definition of the partial derivative. Consider the multivariable function f(x, y). An example of such a function would be elevations above sea level of a geographic region or the concentration of a chemical on a flat surface. To quantify how this function changes with position, we consider two nearby points, f(x, y) and f(x + ∆x, y + ∆y) (Figure C.1). We will also refer to these two points as f x,y (f evaluated at the point (x, y)) and f . | |x+∆x,y+∆y In a two-dimensional function, the “rate of change” is a more complex concept than in a one-dimensional function. For a one-dimensional function, the rate of change of the function f with respect to the variable x was identified with the change in f divided by the change in x, quantified in the derivative, df/dx (see Figure 1.26). For a two-dimensional function, when speaking of the rate of change, we must also specify the direction in which we are interested. For example, if the function we are considering is elevation and we are standing near the edge of a cliff, the rate of change of the elevation in the direction over the cliff is steep, while the rate of change of the elevation in the opposite direction is much more gradual. -
Continuum Mechanics SS 2013
F x₁′ x₁ xₑ xₑ′ x₀′ x₀ F Continuum Mechanics SS 2013 Prof. Dr. Ulrich Schwarz Universität Heidelberg, Institut für theoretische Physik Tel.: 06221-54-9431 EMail: [email protected] Homepage: http://www.thphys.uni-heidelberg.de/~biophys/ Latest Update: July 16, 2013 Address comments and suggestions to [email protected] Contents 1. Introduction 2 2. Linear viscoelasticity in 1d 4 2.1. Motivation . 4 2.2. Elastic response . 5 2.3. Viscous response . 6 2.4. Maxwell model . 7 2.5. Laplace transformation . 9 2.6. Kelvin-Voigt model . 11 2.7. Standard linear model . 12 2.8. Boltzmanns Theory of Linear Viscoelasticity . 14 2.9. Complex modulus . 15 3. Distributed forces in 1d 19 3.1. Continuum equation for an elastic bar . 19 3.2. Elastic chain . 22 4. Elasticity theory in 3d 25 4.1. Material and spatial temporal derivatives . 25 4.2. The displacement vector field . 29 4.3. The strain tensor . 30 4.4. The stress tensor . 33 4.5. Linear elasticity theory . 39 4.6. Non-linear elasticity theory . 41 5. Applications of LET 46 5.1. Reminder on isotropic LET . 46 5.2. Pure Compression . 47 5.3. Pure shear . 47 5.4. Uni-axial stretch . 48 5.5. Biaxial strain . 50 5.6. Elastic cube under its own weight . 51 5.7. Torsion of a bar . 52 5.8. Contact of two elastic spheres (Hertz solution 1881) . 54 5.9. Compatibility conditions . 57 5.10. Bending of a plate . 57 5.11. Bending of a rod . 60 2 1 Contents 6. -
Applied Mathematics Letters a Remark on Jump Conditions for The
Applied Mathematics Letters PERGAMON Applied Mathematics Letters 14 (2001) 149 154 www.elsevier.nl/Iocate/aml A Remark on Jump Conditions for the Three-Dimensional Navier-Stokes Equations Involving an Immersed Moving Membrane MING-CHIH LAI Department of Mathematics, Chung Cheng University Minghsiung, Chiayi 621, Taiwan, R.O.C. mclai©math, ccu. edu. tw ZmUN LI Center for Research in Scientific Computation and Department of Mathematics North Carolina State University, Raleigh, NC 27695-8205, U.S.A. zhilin~math, ncsu. edu (Received March 2000; accepted April 2000) Communicated by A. Nachman Abstract--Jump conditions for the pressure, the velocity, and their normal derivatives across an immersed moving membrane in an incompressible fluid are derived. The discontinuities are due to the singular forces along the membrane. Instead of using the delta function formulation, those jump conditions can be used to formulate the governing equations in an alternative form. It is ~tlso useful for developing more accurate numerical methods such as immersed interface method [or the Navier-Stokes equations involving moving interface. @ 2000 Elsevier Science Ltd. All rights reserved. Keywords--Immersed boundary method, Immersed interface method, Jump conditions. EQUATIONS OF MOTION Problems of biological fluid mechanics often involve an interaction of a viscous incompressible fluid with an elastic moving membrane. One can consider this membrane as a part of the fluid which exerts forces to the fluid and at the same time moves along with the fluid. The mathematical formulation and numerical method for this kind of problem was first introduced by PeskJn to simulate the blood flow through heart valves [1]. -
Hydrogeology and Groundwater Flow
Hydrogeology and Groundwater Flow Hydrogeology (hydro- meaning water, and -geology meaning the study of rocks) is the part of hydrology that deals with the distribution and movement of groundwater in the soil and rocks of the Earth's crust, (commonly in aquifers). The term geohydrology is often used interchangeably. Some make the minor distinction between a hydrologist or engineer applying themselves to geology (geohydrology), and a geologist applying themselves to hydrology (hydrogeology). Hydrogeology (like most earth sciences) is an interdisciplinary subject; it can be difficult to account fully for the chemical, physical, biological and even legal interactions between soil, water, nature and society. Although the basic principles of hydrogeology are very intuitive (e.g., water flows "downhill"), the study of their interaction can be quite complex. Taking into account the interplay of the different facets of a multi-component system often requires knowledge in several diverse fields at both the experimental and theoretical levels. This being said, the following is a more traditional (reductionist viewpoint) introduction to the methods and nomenclature of saturated subsurface hydrology, or simply hydrogeology. © 2014 All Star Training, Inc. 1 Hydrogeology in Relation to Other Fields Hydrogeology, as stated above, is a branch of the earth sciences dealing with the flow of water through aquifers and other shallow porous media (typically less than 450 m or 1,500 ft below the land surface.) The very shallow flow of water in the subsurface (the upper 3 m or 10 ft) is pertinent to the fields of soil science, agriculture and civil engineering, as well as to hydrogeology. -
Geosc 548 Notes R. Dibiase 9/2/2016
Geosc 548 Notes R. DiBiase 9/2/2016 1. Fluid properties and concept of continuum • Fluid: a substance that deforms continuously under an applied shear stress (e.g., air, water, upper mantle...) • Not practical/possible to treat fluid mechanics at the molecular level! • Instead, need to define a representative elementary volume (REV) to average quantities like velocity, density, temperature, etc. within a continuum • Continuum: smoothly varying and continuously distributed body of matter – no holes or discontinuities 1.1 What sets the scale of analysis? • Too small: bad averaging • Too big: smooth over relevant scales of variability… An obvious length scale L for ideal gases is the mean free path (average distance traveled by before hitting another molecule): = ( 1 ) 2 2 where kb is the Boltzman constant, πr is the effective4√2 cross sectional area of a molecule, T is temperature, and P is pressure. Geosc 548 Notes R. DiBiase 9/2/2016 Mean free path of atmosphere Sea level L ~ 0.1 μm z = 50 km L ~ 0.1 mm z = 150 km L ~ 1 m For liquids, not as straightforward to estimate L, but typically much smaller than for gas. 1.2 Consequences of continuum approach Consider a fluid particle in a flow with a gradient in the velocity field : �⃑ For real fluids, some “slow” molecules get caught in faster flow, and some “fast” molecules get caught in slower flow. This cannot be reconciled in continuum approach, so must be modeled. This is the origin of fluid shear stress and molecular viscosity. For gases, we can estimate viscosity from first principles using ideal gas law, calculating rate of momentum exchange directly. -
Selective Energy and Enstrophy Modification of Two-Dimensional
Selective energy and enstrophy modification of two-dimensional decaying turbulence Aditya G. Nair∗, James Hanna & Matteo Aureli Department of Mechanical Engineering, University of Nevada, Reno Abstract In two-dimensional decaying homogeneous isotropic turbulence, kinetic energy and enstrophy are respectively transferred to larger and smaller scales. In such spatiotemporally complex dynamics, it is challenging to identify the important flow structures that govern this behavior. We propose and numerically employ two flow modification strategies that leverage the inviscid global conservation of energy and enstrophy to design external forcing inputs which change these quantities selectively and simultaneously, and drive the system towards steady-state or other late-stage behavior. One strategy employs only local flow-field information, while the other is global. We observe various flow structures excited by these inputs and compare with recent literature. Energy modification is characterized by excitation of smaller wavenumber structures in the flow than enstrophy modification. 1 Introduction Turbulent flows exhibit nonlinear interactions over a wide range of spatiotemporal scales. In two-dimensional (2D) decaying turbulence, the rate of energy dissipation is considerably slowed by kinetic energy transfer to large-scale coherent vortex cores through the inverse energy flux mechanism [2,3,5, 13, 14], while the enstrophy dissipation rate is enhanced by enstrophy transfer to small scale eddies [21]. The identification and modification of collective structures in the flow that accelerate or decelerate the inverse energy flux mechanism or alter the enstrophy cascade is a fundamental question [9, 10]. This is unlikely to be addressed by flow modification strategies based on linearization of the Navier–Stokes equations and reduced-order/surrogate representations that lack strict adherence to conservation laws. -
General Navier-Stokes-Like Momentum and Mass-Energy Equations
General Navier-Stokes-like Momentum and Mass-Energy Equations Jorge Monreal Department of Physics, University of South Florida, Tampa, Florida, USA Abstract A new system of general Navier-Stokes-like equations is proposed to model electromagnetic flow utilizing analogues of hydrodynamic conservation equa- tions. Such equations are intended to provide a different perspective and, potentially, a better understanding of electromagnetic mass, energy and mo- mentum behavior. Under such a new framework additional insights into electromagnetism could be gained. To that end, we propose a system of momentum and mass-energy conservation equations coupled through both momentum density and velocity vectors. Keywords: Navier-Stokes; Electromagnetism; Euler equations; hydrodynamics PACS: 42.25.Dd, 47.10.ab, 47.10.ad 1. Introduction 1.1. System of Navier-Stokes Equations Several groups have applied the Navier-Stokes (NS) equations to Electro- magnetic (EM) fields through analogies of EM field flows to hydrodynamic fluid flow. Most recently, Boriskina and Reinhard made a hydrodynamic analogy utilizing Euler’s approximation to the Navier-Stokes equation in arXiv:1410.6794v2 [physics.class-ph] 29 Aug 2016 order to describe their concept of Vortex Nanogear Transmissions (VNT), which arise from complex electromagnetic interactions in plasmonic nanos- tructures [1]. In 1998, H. Marmanis published a paper that described hydro- dynamic turbulence and made direct analogies between components of the Email address: [email protected] (Jorge Monreal) Preprint submitted to Annals of Physics August 30, 2016 NS equation and Maxwell’s equations of electromagnetism[2]. Kambe for- mulated equations of compressible fluids using analogous Maxwell’s relation and the Euler approximation to the NS equation[3]. -
150A Review Session 2/13/2014 Fluid Statics • • Pressure Acts in All
150A Review Session 2/13/2014 Fluid Statics Pressure acts in all directions, normal to the surrounding surfaces or Whenever a pressure difference is the driving force, use gauge pressure o Bernoulli equation o Momentum balance with Patm everywhere outside Whenever you are looking for the total pressure, use absolute pressure o Force balances Hydrostatic head = pressure from a static column of fluid From a z-direction force balance on a differential cube: o Differential form: use when a variable is changing continuously . Compressible (changing density) fluid, i.e. altitude . Force in x or y direction (changing height), i.e. column support o Integrated form: use when all variables are constant . Total pressure in z direction, i.e. manometer Buoyancy o Recommended to NOT use a “buoyant force” . “Buoyant force” is simply a pressure difference o Do a force balance including all the different pressures & weights . Downward: gravity (W=mg) and atmospheric pressure (Patm*A) . Upward: pressure from fluid below submerged container (ρgΔz*A) 150A Review Session 2/13/2014 Manometers o Pressures are equal at the two points that are at the same height and connected by the same fluid o Work up or down from that equality point, including all fluids (& Patm) Compressible fluids o At constant elevation, from ideal gas law, o 3 ways to account for changing elevation using the ideal gas law . Isothermal ( ) . Linear temperature gradient ( ) . Isentropic ( ) Macroscopic Momentum Balances [Accumulation = In – Out + Generation] for momentum of fluid -
Numerical Modeling of Fluid Interface Phenomena
Numerical Modeling of Fluid Interface Phenomena SARA ZAHEDI Avhandling som med tillst˚andav Kungliga Tekniska h¨ogskolan framl¨aggestill offentlig granskning f¨oravl¨aggandeav teknologie licentiatexamen onsdagen den 10 juni 2009 kl 10:00 i sal D42, Lindstedtsv¨agen5, plan 4, Kungliga Tekniska h¨ogskolan, Stockholm. ISBN 978-91-7415-344-6 TRITA-CSC-A 2009:07 ISSN-1653-5723 ISRN-KTH/CSC/A{09/07-SE c Sara Zahedi, maj 2009 Abstract This thesis concerns numerical techniques for two phase flow simulations; the two phases are immiscible and incompressible fluids. The governing equations are the incompressible Navier{Stokes equations coupled with an evolution equation for interfaces. Strategies for accurate simulations are suggested. In particular, accurate approximations of the surface tension force, and a new model for simulations of contact line dynamics are proposed. In the popular level set methods, the interface that separates two immisci- ble fluids is implicitly defined as a level set of a function; in the standard level set method the zero level set of a signed distance function is used. The surface tension force acting on the interface can be modeled using the delta function with support on the interface. Approximations to such delta functions can be obtained by extending a regularized one{dimensional delta function to higher dimensions using a distance function. However, precaution is needed since it has been shown that this approach can lead to inconsistent approxima- tions. In this thesis we show consistency of this approach for a certain class of one{dimensional delta function approximations. We also propose a new model for simulating contact line dynamics. -
Laminar Flow in Microfluidic Channels
Expo 2007 Laminar Flow in Microfluidic Channels D. Cheng, J. Greenwood, X. Zeng, C. Lo, S. S. Sridharamurthy, L. Dong, Y. Choe, T. Khang, A. Arteaga, and H. Jiang Department of Electrical and Computer Engineering, University of Wisconsin-Madison, USA Madison, WI, Apr. 19th –21st, 2007 Laminar and Turbulent Flow • What is Laminar Flow? – Layers of liquid that flow in a uniform fashion – Layers do not mix with neighboring layers – Opposite of turbulent flow Smooth Rough Laminar Flow Turbulent Flow Laminar vs. Turbulent Flow Sink • A sink can display both laminar and turbulent flow • Lets watch a Movie!!!! Micro Fluidics and Laminar flow • Start with two syringes filled with blue and yellow water Micro Fluidics and Laminar flow • Start to press the liquid into the channel Micro Fluidics and Laminar flow • The fluid star to flow in the Microchannel Micro Fluidics and Laminar flow Flow Chart for Microfluidic channel • It does not mix immediately because it is in laminar flow • This is due to its small size of the channel Reynolds Number and Stokes Flow • Reynolds number is a ratio between inertial force (ρvs) and viscous force (μ/L). http://en.wikipedia.org/wiki/Reynolds_number • Defines if a liquid will be laminar (Reynolds < <1) and turbulent (Reynolds >> 1) flow. • In Microfluidics the Length (L) or Diameter of the channel is what dominates the equation causing a low Reynolds number. – This is also called Stokes flow Large vs. Micro • When dealing with cup of water the dominate force acting on the water is gravity causing the water to be turbulent. • Where as in microchannels gravity is overcome by surface tension and capillary forces. -
Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2019
Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2019 Objective: To introduce the basic concepts of fluid mechanics and heat transfer necessary for solution of engineering/science problems. Text: Required: Welty, Rorrer, and Foster, “Fundamentals of Heat, Mass, and Momentum Transfer,” 6th ed., John Wiley (2015). Recommended: 1. Bird, Stewart, and Lightfoot, “Transport Phenomena,” 2nd ed. John Wiley, NY (2002). 2. Denn, “Process Fluid Mechanics,” Prentice-Hall, NJ (1980). 3. White, “Fluid Mechanics,” 2nd ed. McGraw-Hill, NY (1986). 4. Middleman, “An Introduction to Fluid Dynamics,” Wiley, NY (1998). Description: CBE 150A discusses fluid mechanics and introduces heat transfer: two processes which together with mass transfer (CBE 150B) comprise the field of transport phenomena. Since the transport or movement of momentum, heat and mass is indigenous to all chemical processing, this course is basic to what follows in the curriculum. In other words, this is really a base course of the curriculum. Text coverage is Chapters 1 – 22, excluding Chapter 10. However, lecture material will not necessarily follow the text. Students are expected to have a working knowledge of simple ordinary differential equations and calculus. COURSE SCHEDULE Total Lectures: 40 Week 1: January 23 Concept of Continuum Mechanics, Shell Balance for Statics January 25 Barometric Equation, Manometer Behavior, Archimedes Principle Week 2: January 28 Plane Couette Flow, Streamlines, Stress and Strain, Newtonian fluids, Viscosity Fluxes and driving -
Extremum Principles for Slow Viscous Flows with Applications to Suspensions
J. Fluid Mech. (1967), vol. 30, part 1, pp. 97-125 97 Printed in Great Britain Extremum principles for slow viscous flows with applications to suspensions By JOSEPH B. KELLER, LESTER A. RUBENFELD https://doi.org/10.1017/S0022112067001326 Courant Institute of Mathematical Sciences, New York University, . New York, N.Y. AND JOHN E. MOLYNEUX Department of Mechanical and Aerospace Sciences, University of Rochester, Rochester, N.Y. (Received 9 January 1967) Helmholtz stated and Korteweg proved that of all divergenceless velocity fields https://www.cambridge.org/core/terms in a domain, with prescribed values on the boundary, the solution of the Stokes equation minimizes the rate of viscous energy dissipation. Hill & Power and also Kearsley proved the corresponding reciprocal maximum principle involving the stress tensor. We prove generalizations of both these principles to the flow of a liquid containing one or more solid bodies and drops of another liquid. The essential point in doing this is to take account of the motion of the solids or drops, which must be determined along with the flow. We illustrate the use of these principles by deducing several consequences from them. In particular we obtain upper and lower bounds on the effective coefficient of viscosity and a lower bound on the sedimentation velocity of suspensions of any concentration. The results involve the statistical properties of the distribution of suspended particles or drops. Graphs of the bounds are shown for special cases. For very low concentra- tions of spheres, both bounds on the effective viscosity coefficient are the same, , subject to the Cambridge Core terms of use, available at and agree with the results of Einstein and Taylor.