Microscopic Momentum Balance Equation (Navier-Stokes)
|
|
- Jared Horton
- 5 years ago
- Views:
Transcription
1 CM3110 Transport I Part I: Fluid Mechanics Microscopic Momentum Balance Equation (Naier-Stokes) Professor Faith Morrison Department of Chemical Engineering Michigan Technological Uniersity 1 Microscopic Balances We hae been doing a microscopic control olume balance; these are specific to whateer problem we are soling. We seek equations for microscopic mass, momentum (and energy) balances that are general. equations must not depend on the choice of the control olume, dx d dy equations must capture the appropriate balance 1
2 Arbitrary Control olume in a Flow b `` S ds nˆ V Mass Balance On an arbitrary control olume:.. (details in the book) ate of increase of mass Net conection in (just as we did with the indiidual control olume balance) Microscopic mass balance for any flow
3 Continuity Equation ds S nˆ Microscopic mass balance written on an arbitrarily shaped control olume, V, enclosed by a surface, S V t x x y y x x y y Microscopic mass balance is a scalar equation. Gibbs notation: t 5 Momentum Balance On an arbitrary control olume: (details in the book) V t dv dv g dv ate of increase of momentum (just as we did with the indiidual control olume balance) V Net conection in Microscopic momentum balance for any flow V Force due to graity V dv Viscous forces and pressure forces 3
4 Equation of Motion S ds nˆ V microscopic momentum balance written on an arbitrarily shaped control olume, V, enclosed by a surface, S Gibbs notation: Gibbs notation: P g t P t Naier Stokes Equation g general fluid Newtonian fluid Microscopic momentum balance is a ector equation. 7 Continuity Equation (And Non Newtonian Equation) on the FONT t The one with is for non Newtonian fluids Faith A. Morrison, Michigan 8 4
5 Naier Stokes (Newtonian Fluids Only) is on the back: P t g 9 Problem Soling Procedure soling for elocity and stress fields 1. sketch system. choose coordinate system amended: when using the microscopic balances 3. simplify the continuity equation (mass balance) 4. simplify the 3 components of the equation of motion (momentum balance) (note that for a Newtonian fluid, the equation of motion is the Naier Stokes equation) 5. sole the differential equations for elocity and pressure (if applicable) 6. apply boundary conditions 7. calculate any engineering alues of interest (flow rate, aerage elocity, force on wall) T 10 5
6 EXAMPLE I: Flow of a Newtonian fluid down an inclined plane eisited g x g sin x x x g g cos air H fluid g g g g g x y g sin 0 g cos 11 EXAMPLE I: Flow of a Newtonian fluid down an inclined plane eisited (see hand notes) 1 6
7 As with balance we performed with a control olume we selected, we made modelling assumptions along the way that we can collect and associate with the final result: Model Assumptions: (laminar flow down an incline, Newtonian) 1. no elocity in the x or y directions (laminar flow). well deeloped flow no edge effects in y direction (width) 4. constant density 5. steady state 6. Newtonian fluid 7. no shear stress at interface 8. no slip at wall 13 A r cross-section A: r L (r) EXAMPLE II: Pressure drien flow of a Newtonian fluid in a tube: (Poiseuille flow) steady state constant well deeloped long tube pressure at top pressure at bottom fluid g 14 7
8 15 Naier Stokes:
9 See hand notes 17 List of Common Integrals 014CommonIntegrals.pdf 18 9
10 What is the force on the walls in this flow? Total wetted area force area cross-section A: r (r) L Inside surface of tube?? fluid 19 9 stresses at a point in space y kg m s force kg m / s y area area s area / Momentum Flux f ê y f A( eˆ eˆ yy yx y x eˆ ) y A surface whose unit normal is in the y-direction stress on a y-surface in the y-direction (See discussion of sign conention of stress; this is the tension positie conention) in the -direction y flux of -momentum 0 10
11 What is the shear stress in this flow? Stress on an surface in the direction cross-section A: r L (r) fluid 1 Force on the walls: See hand notes 11
12 4 1 3 Engineering Quantities of Interest (tube flow) aerage elocity olumetric flow rate component of force on the wall Q rdr d rdr d rdr d Must work these out for each problem in the coordinate system in use; see inside back coer of book. 4 1
13 Engineering Quantities of Interest (any flow) olumetric flow rate aerage elocity component of force on the wall For more complex flows, we use the Gibbs notation ersions (will discuss soon) Hagen Poiseuille Equation** 6 13
14 a 0 0,max r rdrd Lg P 4L o Lg P 8L o P L P L r rdrd 7 a 1.5 p p 0 p p 0 L L Velocity maximum is twice the aerage (for incline it was.5 the aerage) r 8 14
15 EXAMPLE II: Pressure drien flow of a Newtonian fluid in a tube: Poiseuille flow /<> Bullet shaped; flow down an incline was parabola, but a sheet. 9 Can this modeling method work for complex flows? Answer: yes. (with some qualifiers) 30 15
Microscopic Momentum Balance Equation (Navier-Stokes)
CM3110 Transport I Part I: Fluid Mechanics Microscopic Momentum Balance Equation (Navier-Stokes) Professor Faith Morrison Department of Chemical Engineering Michigan Technological University 1 Microscopic
More informationds nˆ v x v t v y Microscopic Balances 10/3/2011
Microscopic Balances We hae been doing microscopic shell hllbl balances that t are specific to whateer problem we are soling. We seek equations for microscopic mass, momentum (and energy) balances that
More informationMicroscopic Momentum Balances
013 Fluids ectue 6 7 Moison CM3110 10//013 CM3110 Tanspot I Pat I: Fluid Mechanics Micoscopic Momentum Balances Pofesso Faith Moison Depatment of Chemical Engineeing Michigan Technological Uniesity 1 Micoscopic
More informationWhat we know about Fluid Mechanics. What we know about Fluid Mechanics
What we know about Fluid Mechanics 1. Survey says. 3. Image from: www.axs.com 4. 5. 6. 1 What we know about Fluid Mechanics 1. MEB (single input, single output, steady, incompressible, no rxn, no phase
More informationChapter 3: Newtonian Fluids
Chapter 3: Newtonian Fluids CM4650 Michigan Tech Navier-Stokes Equation v vv p t 2 v g 1 Chapter 3: Newtonian Fluid TWO GOALS Derive governing equations (mass and momentum balances Solve governing equations
More informationShell Balances in Fluid Mechanics
Shell Balances in Fluid Mechanics R. Shankar Subramanian Department of Chemical and Biomolecular Engineering Clarkson University When fluid flow occurs in a single direction everywhere in a system, shell
More informationChapter 8 Laminar Flows with Dependence on One Dimension
Chapter 8 Laminar Flows with Dependence on One Dimension Couette low Planar Couette low Cylindrical Couette low Planer rotational Couette low Hele-Shaw low Poiseuille low Friction actor and Reynolds number
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 informationFlux - definition: (same format for all types of transport, momentum, energy, mass)
Fundamentals of Transport Flu - definition: (same format for all types of transport, momentum, energy, mass) flu in a given direction Quantity of property being transferred ( time)( area) More can be transported
More informationPHY121 Physics for the Life Sciences I
PHY Physics for the Life Sciences I Lecture 0. Fluid flow: kinematics describing the motion. Fluid flow: dynamics causes and effects, Bernoulli s Equation 3. Viscosity and Poiseuille s Law for narrow tubes
More informationBasic Fluid Mechanics
Basic Fluid Mechanics Chapter 3B: Conservation of Mass C3B: Conservation of Mass 1 3.2 Governing Equations There are two basic types of governing equations that we will encounter in this course Differential
More informationChapter 5. The Differential Forms of the Fundamental Laws
Chapter 5 The Differential Forms of the Fundamental Laws 1 5.1 Introduction Two primary methods in deriving the differential forms of fundamental laws: Gauss s Theorem: Allows area integrals of the equations
More informationGetting started: CFD notation
PDE of p-th order Getting started: CFD notation f ( u,x, t, u x 1,..., u x n, u, 2 u x 1 x 2,..., p u p ) = 0 scalar unknowns u = u(x, t), x R n, t R, n = 1,2,3 vector unknowns v = v(x, t), v R m, m =
More informationAE/ME 339. K. M. Isaac Professor of Aerospace Engineering. 12/21/01 topic7_ns_equations 1
AE/ME 339 Professor of Aerospace Engineering 12/21/01 topic7_ns_equations 1 Continuity equation Governing equation summary Non-conservation form D Dt. V 0.(2.29) Conservation form ( V ) 0...(2.33) t 12/21/01
More informationChapter 9: Differential Analysis
9-1 Introduction 9-2 Conservation of Mass 9-3 The Stream Function 9-4 Conservation of Linear Momentum 9-5 Navier Stokes Equation 9-6 Differential Analysis Problems Recall 9-1 Introduction (1) Chap 5: Control
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 informationMacroscopic Momentum Balances
Lecture 13 F. Morrson CM3110 2013 10/22/2013 CM3110 Transport I Part I: Flud Mechancs Macroscopc Momentum Balances Professor Fath Morrson Department of Chemcal Engneerng Mchgan Technologcal Unersty 1 Macroscopc
More informationBoundary Conditions in Fluid Mechanics
Boundary Conditions in Fluid Mechanics R. Shankar Subramanian Department of Chemical and Biomolecular Engineering Clarkson University The governing equations for the velocity and pressure fields are partial
More informationViscosity and Polymer Melt Flow. Rheology-Processing / Chapter 2 1
Viscosity and Polymer Melt Flow Rheology-Processing / Chapter 2 1 Viscosity: a fluid property resistance to flow (a more technical definition resistance to shearing) Remember that: τ μ du dy shear stress
More information150A Review Session 2/13/2014 Fluid Statics. Pressure acts in all directions, normal to the surrounding surfaces
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
More informationChapter 2: 1D Kinematics Tuesday January 13th
Chapter : D Kinematics Tuesday January 3th Motion in a straight line (D Kinematics) Aerage elocity and aerage speed Instantaneous elocity and speed Acceleration Short summary Constant acceleration a special
More informationChapter 6: Momentum Analysis
6-1 Introduction 6-2Newton s Law and Conservation of Momentum 6-3 Choosing a Control Volume 6-4 Forces Acting on a Control Volume 6-5Linear Momentum Equation 6-6 Angular Momentum 6-7 The Second Law of
More informationVISUAL PHYSICS ONLINE RECTLINEAR MOTION: UNIFORM ACCELERATION
VISUAL PHYSICS ONLINE RECTLINEAR MOTION: UNIFORM ACCELERATION Predict Obsere Explain Exercise 1 Take an A4 sheet of paper and a heay object (cricket ball, basketball, brick, book, etc). Predict what will
More informationFORMULA SHEET. General formulas:
FORMULA SHEET You may use this formula sheet during the Advanced Transport Phenomena course and it should contain all formulas you need during this course. Note that the weeks are numbered from 1.1 to
More informationFluid Mechanics Qualifying Examination Sample Exam 2
Fluid Mechanics Qualifying Examination Sample Exam 2 Allotted Time: 3 Hours The exam is closed book and closed notes. Students are allowed one (double-sided) formula sheet. There are five questions on
More informationSLIP MODEL PERFORMANCE FOR MICRO-SCALE GAS FLOWS
3th AIAA Thermophysics Conference 3- June 3, Orlando, Florida AIAA 3-5 SLIP MODEL PERFORMANCE FOR MICRO-SCALE GAS FLOWS Matthew J. McNenly* Department of Aerospace Engineering Uniersity of Michigan, Ann
More informationUNDERSTAND MOTION IN ONE AND TWO DIMENSIONS
SUBAREA I. COMPETENCY 1.0 UNDERSTAND MOTION IN ONE AND TWO DIMENSIONS MECHANICS Skill 1.1 Calculating displacement, aerage elocity, instantaneous elocity, and acceleration in a gien frame of reference
More informationDifferential relations for fluid flow
Differential relations for fluid flow In this approach, we apply basic conservation laws to an infinitesimally small control volume. The differential approach provides point by point details of a flow
More informationChapter 3: Newtonian Fluid Mechanics QUICK START W
Chapter 3: Newtonian Fluid Mechanics TWO GOAL Derive governing equations (mass and momentum balances olve governing equations or velocity and stress ields QUICK TART W First, beore we get deep into derivation,
More informationSection 2: Lecture 1 Integral Form of the Conservation Equations for Compressible Flow
Section 2: Lecture 1 Integral Form of the Conservation Equations for Compressible Flow Anderson: Chapter 2 pp. 41-54 1 Equation of State: Section 1 Review p = R g T " > R g = R u M w - R u = 8314.4126
More informationvs. Chapter 4: Standard Flows Chapter 4: Standard Flows for Rheology shear elongation 2/1/2016 CM4650 Lectures 1-3: Intro, Mathematical Review
CM465 Lectures -3: Intro, Mathematical //6 Chapter 4: Standard Flows CM465 Polymer Rheology Michigan Tech Newtonian fluids: vs. non-newtonian fluids: How can we investigate non-newtonian behavior? CONSTANT
More informationESCI 485 Air/sea Interaction Lesson 3 The Surface Layer
ESCI 485 Air/sea Interaction Lesson 3 he Surface Layer References: Air-sea Interaction: Laws and Mechanisms, Csanady Structure of the Atmospheric Boundary Layer, Sorbjan HE PLANEARY BOUNDARY LAYER he atmospheric
More informationSupplementary Information Microfluidic quadrupole and floating concentration gradient Mohammad A. Qasaimeh, Thomas Gervais, and David Juncker
Mohammad A. Qasaimeh, Thomas Gerais, and Daid Juncker Supplementary Figure S1 The microfluidic quadrupole (MQ is modeled as two source (Q inj and two drain (Q asp points arranged in the classical quardupolar
More informationMA3D1 Fluid Dynamics Support Class 5 - Shear Flows and Blunt Bodies
MA3D1 Fluid Dynamics Support Class 5 - Shear Flows and Blunt Bodies 13th February 2015 Jorge Lindley email: J.V.M.Lindley@warwick.ac.uk 1 2D Flows - Shear flows Example 1. Flow over an inclined plane A
More informationREE Internal Fluid Flow Sheet 2 - Solution Fundamentals of Fluid Mechanics
REE 307 - Internal Fluid Flow Sheet 2 - Solution Fundamentals of Fluid Mechanics 1. Is the following flows physically possible, that is, satisfy the continuity equation? Substitute the expressions for
More informationThe Kinetic Theory of Gases
978-1-107-1788-3 Classical and Quantum Thermal Physics The Kinetic Theory of Gases CHAPTER 1 1.0 Kinetic Theory, Classical and Quantum Thermodynamics Two important components of the unierse are: the matter
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 informationCJ57.P.003 REASONING AND SOLUTION According to the impulse-momentum theorem (see Equation 7.4), F t = mv
Solution to HW#7 CJ57.CQ.003. RASONNG AND SOLUTON a. Yes. Momentum is a ector, and the two objects hae the same momentum. This means that the direction o each object s momentum is the same. Momentum is
More informationAE/ME 339. Computational Fluid Dynamics (CFD) K. M. Isaac. Momentum equation. Computational Fluid Dynamics (AE/ME 339) MAEEM Dept.
AE/ME 339 Computational Fluid Dynamics (CFD) 9//005 Topic7_NS_ F0 1 Momentum equation 9//005 Topic7_NS_ F0 1 Consider the moving fluid element model shown in Figure.b Basis is Newton s nd Law which says
More informationChapter 2: Fluid Dynamics Review
7 Chapter 2: Fluid Dynamics Review This chapter serves as a short review of basic fluid mechanics. We derive the relevant transport equations (or conservation equations), state Newton s viscosity law leading
More information(a) During the first part of the motion, the displacement is x 1 = 40 km and the time interval is t 1 (30 km / h) (80 km) 40 km/h. t. (2.
Chapter 3. Since the trip consists of two parts, let the displacements during first and second parts of the motion be x and x, and the corresponding time interals be t and t, respectiely. Now, because
More information0 a 3 a 2 a 3 0 a 1 a 2 a 1 0
Chapter Flow kinematics Vector and tensor formulae This introductory section presents a brief account of different definitions of ector and tensor analysis that will be used in the following chapters.
More informationPHYS 1443 Section 004 Lecture #4 Thursday, Sept. 4, 2014
PHYS 1443 Section 004 Lecture #4 Thursday, Sept. 4, 014 One Dimensional Motion Motion under constant acceleration One dimensional Kinematic Equations How do we sole kinematic problems? Falling motions
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 informationBOUNDARY LAYER ANALYSIS WITH NAVIER-STOKES EQUATION IN 2D CHANNEL FLOW
Proceedings of,, BOUNDARY LAYER ANALYSIS WITH NAVIER-STOKES EQUATION IN 2D CHANNEL FLOW Yunho Jang Department of Mechanical and Industrial Engineering University of Massachusetts Amherst, MA 01002 Email:
More informationr t t x t y t z t, y t are zero, then construct a table for all four functions. dy dx 0 and 0 dt dt horizontal tangent vertical tangent
3. uggestions for the Formula heets Below are some suggestions for many more formulae than can be placed easily on both sides of the two standard 8½"" sheets of paper for the final examination. It is strongly
More informationLesson 10 Steady Electric Currents
Lesson Steady lectric Currents 楊尚達 Shang-Da Yang Institute of Photonics Technologies Department of lectrical ngineering National Tsing Hua Uniersity, Taiwan Outline Current density Current laws Boundary
More informationChapter 6: Momentum Analysis of Flow Systems
Chapter 6: Momentum Analysis of Flow Systems Introduction Fluid flow problems can be analyzed using one of three basic approaches: differential, experimental, and integral (or control volume). In Chap.
More informationAA210A Fundamentals of Compressible Flow. Chapter 5 -The conservation equations
AA210A Fundamentals of Compressible Flow Chapter 5 -The conservation equations 1 5.1 Leibniz rule for differentiation of integrals Differentiation under the integral sign. According to the fundamental
More informationME 509, Spring 2016, Final Exam, Solutions
ME 509, Spring 2016, Final Exam, Solutions 05/03/2016 DON T BEGIN UNTIL YOU RE TOLD TO! Instructions: This exam is to be done independently in 120 minutes. You may use 2 pieces of letter-sized (8.5 11
More informationFeb 6, 2013 PHYSICS I Lecture 5
95.141 Feb 6, 213 PHYSICS I Lecture 5 Course website: faculty.uml.edu/pchowdhury/95.141/ www.masteringphysics.com Course: UML95141SPRING213 Lecture Capture h"p://echo36.uml.edu/chowdhury213/physics1spring.html
More informationENGI Gradient, Divergence, Curl Page 5.01
ENGI 94 5. - Gradient, Divergence, Curl Page 5. 5. The Gradient Operator A brief review is provided here for the gradient operator in both Cartesian and orthogonal non-cartesian coordinate systems. Sections
More informationCM3110 Transport Processes and Unit Operations I
CM3110 Transport Processes and Unit Operations I Professor Faith Morrison Department of Chemical Engineering Michigan Technological University CM3110 - Momentum and Heat Transport CM310 Heat and Mass Transport
More informationCENG 501 Examination Problem: Estimation of Viscosity with a Falling - Cylinder Viscometer
CENG 501 Examination Problem: Estimation of Viscosity with a Falling - Cylinder Viscometer You are assigned to design a fallingcylinder viscometer to measure the viscosity of Newtonian liquids. A schematic
More informationChapter 2 Motion Along a Straight Line
Chapter Motion Along a Straight Line In this chapter we will study how objects moe along a straight line The following parameters will be defined: (1) Displacement () Aerage elocity (3) Aerage speed (4)
More informationCHAPTER 4 ANALYTICAL SOLUTIONS OF COUPLE STRESS FLUID FLOWS THROUGH POROUS MEDIUM BETWEEN PARALLEL PLATES WITH SLIP BOUNDARY CONDITIONS
CHAPTER 4 ANALYTICAL SOLUTIONS OF COUPLE STRESS FLUID FLOWS THROUGH POROUS MEDIUM BETWEEN PARALLEL PLATES WITH SLIP BOUNDARY CONDITIONS Introduction: The objective of this chapter is to establish analytical
More informationPart 2: CM3110 Transport Processes and Unit Operations I. Professor Faith Morrison. CM2110/CM Review. Concerned now with rates of heat transfer
CM30 anspot Pocesses and Unit Opeations I Pat : Pofesso Fait Moison Depatment of Cemical Engineeing Micigan ecnological Uniesity CM30 - Momentum and Heat anspot CM30 Heat and Mass anspot www.cem.mtu.edu/~fmoiso/cm30/cm30.tml
More informationTHE EFFECT OF LONGITUDINAL VIBRATION ON LAMINAR FORCED CONVECTION HEAT TRANSFER IN A HORIZONTAL TUBE
mber 3 Volume 3 September 26 Manal H. AL-Hafidh Ali Mohsen Rishem Ass. Prof. /Uniersity of Baghdad Mechanical Engineer ABSTRACT The effect of longitudinal ibration on the laminar forced conection heat
More informationPh.D. Qualifying Exam in Fluid Mechanics
Student ID Department of Mechanical Engineering Michigan State University East Lansing, Michigan Ph.D. Qualifying Exam in Fluid Mechanics Closed book and Notes, Some basic equations are provided on an
More informationAE/ME 339. K. M. Isaac. 9/22/2005 Topic 6 FluidFlowEquations_Introduction. Computational Fluid Dynamics (AE/ME 339) MAEEM Dept.
AE/ME 339 Computational Fluid Dynamics (CFD) 1...in the phrase computational fluid dynamics the word computational is simply an adjective to fluid dynamics.... -John D. Anderson 2 1 Equations of Fluid
More information- Marine Hydrodynamics. Lecture 4. Knowns Equations # Unknowns # (conservation of mass) (conservation of momentum)
2.20 - Marine Hydrodynamics, Spring 2005 Lecture 4 2.20 - Marine Hydrodynamics Lecture 4 Introduction Governing Equations so far: Knowns Equations # Unknowns # density ρ( x, t) Continuity 1 velocities
More informationLecture 12! Center of mass! Uniform circular motion!
Lecture 1 Center of mass Uniform circular motion Today s Topics: Center of mass Uniform circular motion Centripetal acceleration and force Banked cures Define the center of mass The center of mass is a
More informationPage 1. Neatly print your name: Signature: (Note that unsigned exams will be given a score of zero.)
Page 1 Neatly print your name: Signature: (Note that unsigned exams will be given a score of zero.) Circle your lecture section (-1 point if not circled, or circled incorrectly): Prof. Vlachos Prof. Ardekani
More informationFLUID FLOW AND HEAT TRANSFER IN A COLLAPSIBLE TUBE
FLUID DYNAMICS FLUID FLOW AND HEAT TRANSFER IN A COLLAPSIBLE TUBE S. A. ODEJIDE 1, Y. A. S. AREGBESOLA 1, O. D. MAKINDE 1 Obafemi Awolowo Uniersity, Department of Mathematics, Faculty of Science, Ile-Ife,
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 information6.1 Steady, One-Dimensional Rectilinear Flows Steady, Spherically Symmetric Radial Flows 42
Contents 6 UNIDIRECTIONAL FLOWS 1 6.1 Steady, One-Dimensional Rectilinear Flows 6. Steady, Axisymmetric Rectilinear Flows 19 6.3 Steady, Axisymmetric Torsional Flows 8 6.4 Steady, Axisymmetric Radial Flows
More informationExercise 5: Exact Solutions to the Navier-Stokes Equations I
Fluid Mechanics, SG4, HT009 September 5, 009 Exercise 5: Exact Solutions to the Navier-Stokes Equations I Example : Plane Couette Flow Consider the flow of a viscous Newtonian fluid between two parallel
More informationPrediction of Coating Thickness
Prediction of Coating Tickness Jon D. Wind Surface Penomena CE 385M 4 May 1 Introduction Tis project involves te modeling of te coating of metal plates wit a viscous liquid by pulling te plate vertically
More informationIn this section, mathematical description of the motion of fluid elements moving in a flow field is
Jun. 05, 015 Chapter 6. Differential Analysis of Fluid Flow 6.1 Fluid Element Kinematics In this section, mathematical description of the motion of fluid elements moving in a flow field is given. A small
More information4 Fundamentals of Continuum Thermomechanics
4 Fundamentals of Continuum Thermomechanics In this Chapter, the laws of thermodynamics are reiewed and formulated for a continuum. The classical theory of thermodynamics, which is concerned with simple
More informationNote: the net distance along the path is a scalar quantity its direction is not important so the average speed is also a scalar.
PHY 309 K. Solutions for the first mid-term test /13/014). Problem #1: By definition, aerage speed net distance along the path of motion time. 1) ote: the net distance along the path is a scalar quantity
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 informationFLUID MECHANICS EQUATIONS
FLUID MECHANIC EQUATION M. Ragheb 11/2/2017 INTRODUCTION The early part of the 18 th -century saw the burgeoning of the field of theoretical fluid mechanics pioneered by Leonhard Euler and the father and
More information2 Law of conservation of energy
1 Newtonian viscous Fluid 1 Newtonian fluid For a Newtonian we already have shown that σ ij = pδ ij + λd k,k δ ij + 2µD ij where λ and µ are called viscosity coefficient. For a fluid under rigid body motion
More informationDetailed Outline, M E 521: Foundations of Fluid Mechanics I
Detailed Outline, M E 521: Foundations of Fluid Mechanics I I. Introduction and Review A. Notation 1. Vectors 2. Second-order tensors 3. Volume vs. velocity 4. Del operator B. Chapter 1: Review of Basic
More informationCIRCULAR MOTION EXERCISE 1 1. d = rate of change of angle
CICULA MOTION EXECISE. d = rate of change of angle as they both complete angle in same time.. c m mg N r m N mg r Since r A r B N A N B. a Force is always perpendicular to displacement work done = 0 4.
More informationCOMPARISON OF ANALYTICAL SOLUTIONS FOR CMSMPR CRYSTALLIZER WITH QMOM POPULATION BALANCE MODELING IN FLUENT
CHINA PARTICUOLOGY Vol. 3, No. 4, 13-18, 5 COMPARISON OF ANALYTICAL SOLUTIONS FOR CMSMPR CRYSTALLIZER WITH QMOM POPULATION BALANCE MODELING IN FLUENT Bin Wan 1, Terry A. Ring 1, *, Kumar M. Dhanasekharan
More informationKinetic plasma description
Kinetic plasma description Distribution function Boltzmann and Vlaso equations Soling the Vlaso equation Examples of distribution functions plasma element t 1 r t 2 r Different leels of plasma description
More informationPhysics 11 HW #7 Solutions
hysics HW #7 Solutions Chapter 7: Focus On Concepts: 2, 6, 0, 3 robles: 8, 7, 2, 22, 32, 53, 56, 57 Focus On Concepts 7-2 (d) Moentu is a ector quantity that has a agnitude and a direction. The agnitudes
More informationConservation of Mass. Computational Fluid Dynamics. The Equations Governing Fluid Motion
http://www.nd.edu/~gtryggva/cfd-course/ http://www.nd.edu/~gtryggva/cfd-course/ Computational Fluid Dynamics Lecture 4 January 30, 2017 The Equations Governing Fluid Motion Grétar Tryggvason Outline Derivation
More informationa by a factor of = 294 requires 1/T, so to increase 1.4 h 294 = h
IDENTIFY: If the centripetal acceleration matches g, no contact force is required to support an object on the spinning earth s surface. Calculate the centripetal (radial) acceleration /R using = πr/t to
More informationFluid Dynamics for Ocean and Environmental Engineering Homework #2 Viscous Flow
OCEN 678-600 Fluid Dynamics for Ocean and Environmental Engineering Homework #2 Viscous Flow Date distributed : 9.18.2005 Date due : 9.29.2005 at 5:00 pm Return your solution either in class or in my mail
More informationHomework #4 Solution. μ 1. μ 2
Homework #4 Solution 4.20 in Middleman We have two viscous liquids that are immiscible (e.g. water and oil), layered between two solid surfaces, where the top boundary is translating: y = B y = kb y =
More informationMath 212-Lecture 20. P dx + Qdy = (Q x P y )da. C
15. Green s theorem Math 212-Lecture 2 A simple closed curve in plane is one curve, r(t) : t [a, b] such that r(a) = r(b), and there are no other intersections. The positive orientation is counterclockwise.
More informationP = 1 3 (σ xx + σ yy + σ zz ) = F A. It is created by the bombardment of the surface by molecules of fluid.
CEE 3310 Thermodynamic Properties, Aug. 27, 2010 11 1.4 Review A fluid is a substance that can not support a shear stress. Liquids differ from gasses in that liquids that do not completely fill a container
More informationOn my honor, I have neither given nor received unauthorized aid on this examination.
Instructor(s): Field/Furic PHYSICS DEPARTENT PHY 2053 Exam 1 October 5, 2011 Name (print, last first): Signature: On my honor, I hae neither gien nor receied unauthorized aid on this examination. YOUR
More informationReview for Exam Hyunse Yoon, Ph.D. Adjunct Assistant Professor Department of Mechanical Engineering, University of Iowa
Review for Exam2 11. 13. 2015 Hyunse Yoon, Ph.D. Adjunct Assistant Professor Department of Mechanical Engineering, University of Iowa Assistant Research Scientist IIHR-Hydroscience & Engineering, University
More informationFOCUS ON CONCEPTS Section 7.1 The Impulse Momentum Theorem
WEEK-6 Recitation PHYS 3 FOCUS ON CONCEPTS Section 7. The Impulse Momentum Theorem Mar, 08. Two identical cars are traeling at the same speed. One is heading due east and the other due north, as the drawing
More informationNote on Posted Slides. Motion Is Relative
Note on Posted Slides These are the slides that I intended to show in class on Tue. Jan. 9, 2014. They contain important ideas and questions from your reading. Due to time constraints, I was probably not
More informationPrediction of anode arc root position in a DC arc plasma torch
Prediction of anode arc root position in a DC arc plasma torch He-Ping Li 1, E. Pfender 1, Xi Chen 1 Department of Mechanical Engineering, Uniersity of Minnesota, Minneapolis, MN 55455, USA Department
More informationFLUID MECHANICS. Chapter 9 Flow over Immersed Bodies
FLUID MECHANICS Chapter 9 Flow over Immersed Bodies CHAP 9. FLOW OVER IMMERSED BODIES CONTENTS 9.1 General External Flow Characteristics 9.3 Drag 9.4 Lift 9.1 General External Flow Characteristics 9.1.1
More informationUniversity of Washington Department of Chemistry Chemistry 453 Winter Quarter 2013
Lecture 1 3/13/13 University of Washington Department of Chemistry Chemistry 53 Winter Quarter 013 A. Definition of Viscosity Viscosity refers to the resistance of fluids to flow. Consider a flowing liquid
More informationChapter 4 Continuity Equation and Reynolds Transport Theorem
Chapter 4 Continuity Equation and Reynolds Transport Theorem 4.1 Control Volume 4. The Continuity Equation for One-Dimensional Steady Flow 4.3 The Continuity Equation for Two-Dimensional Steady Flow 4.4
More informationPIPE FLOWS: LECTURE /04/2017. Yesterday, for the example problem Δp = f(v, ρ, μ, L, D) We came up with the non dimensional relation
/04/07 ECTURE 4 PIPE FOWS: Yesterday, for the example problem Δp = f(v, ρ, μ,, ) We came up with the non dimensional relation f (, ) 3 V or, p f(, ) You can plot π versus π with π 3 as a parameter. Or,
More informationSPACE-TIME HOLOMORPHIC TIME-PERIODIC SOLUTIONS OF NAVIER-STOKES EQUATIONS. 1. Introduction We study Navier-Stokes equations in Lagrangean coordinates
Electronic Journal of Differential Equations, Vol. 2013 2013, No. 218, pp. 1 5. ISSN: 1072-6691. URL: http://ejde.math.txstate.edu or http://ejde.math.unt.edu ftp ejde.math.txstate.edu SPACE-TIME HOLOMORPHIC
More informationMCAT Physics - Problem Drill 06: Translational Motion
MCAT Physics - Problem Drill 06: Translational Motion Question No. 1 of 10 Instructions: (1) Read the problem and answer choices carefully () Work the problems on paper as 1. An object falls from rest
More informationBasic Fluid Mechanics
Basic Fluid Mechanics Chapter 6A: Internal Incompressible Viscous Flow 4/16/2018 C6A: Internal Incompressible Viscous Flow 1 6.1 Introduction For the present chapter we will limit our study to incompressible
More informationChapter 2: Basic Governing Equations
-1 Reynolds Transport Theorem (RTT) - Continuity Equation -3 The Linear Momentum Equation -4 The First Law of Thermodynamics -5 General Equation in Conservative Form -6 General Equation in Non-Conservative
More informationAMME2261: Fluid Mechanics 1 Course Notes
Module 1 Introduction and Fluid Properties Introduction Matter can be one of two states: solid or fluid. A fluid is a substance that deforms continuously under the application of a shear stress, no matter
More informationFLOW-FORCE COMPENSATION IN A HYDRAULIC VALVE
FLOW-FORCE COMPENSATION IN A HYDRAULIC VALVE Jan Lugowski Purdue Uniersity West Lafayette, IN, USA lugowskj@purdue.edu ABSTRACT Flow-reaction forces acting in hydraulic ales hae been studied for many decades.
More information