Aula Teórica 17 Equação de Evolução da Energia Mecânica.

Slides:



Advertisements
Similar presentations
Boundary layer with pressure gradient in flow direction.
Advertisements

_______________________________________________ LECTURE 9 Hydraulic machines III and EM machines ________________________________________ © 2002 MIT PSDAM.
Aula Teórica 11 Integral Budgets: Momentum. General Principle & Mass The rate of accumulation inside a Control Volume balances the fluxes plus production.
Escoamento de Couette, i.e., escoamento entre duas placas planas.
Aula Teórica 17 Equações em coordenadas cilíndricas. Força centrífuga, força de coriolis e escoamento laminar num tubo cilíndico.
11 th International Conference on Pressure Surges Lisbon, Portugal, 24 – 26 October 2012 Evaluation of flow resistance in unsteady pipe.
Aula Teórica 8 Equação de Bernoulli. Bernoulli’s Equation Let us consider a Stream - pipe such as indicated in the figure and an ideal fluid (without.
Exercices Lecture 8. The boat is moving and consequently the control volume must be moving with it. The flow entering into the control volume is the flow.
Lecture 15: Capillary motion
Chapter 2 Introduction to Heat Transfer
Convection.
Shell Momentum Balances
Conservation of Linear Momentum.
Pharos University ME 352 Fluid Mechanics II
Example: Exercise (Pump)
ME 259 Fluid Mechanics for Electrical Students
Flow over an Obstruction MECH 523 Applied Computational Fluid Dynamics Presented by Srinivasan C Rasipuram.
Fluid Dynamics.
CHE/ME 109 Heat Transfer in Electronics LECTURE 17 – INTERNAL FORCED CONVECTION FUNDAMENTALS.
Formula sheet No explanation is made on purpose Do not assume that you need to use every formula In this test always assume that K entrance = 0.5, K exit.
MECH 221 FLUID MECHANICS (Fall 06/07) Chapter 9: FLOWS IN PIPE
D A C B z = 20m z=4m Homework Problem A cylindrical vessel of height H = 20 m is filled with water of density to a height of 4m. What is the pressure at:
CIEG 305 DERIVATION OF THE ENERGY EQUATION 1 st Law of Thermodynamics Change in energy per time Rate at which heat is added to system Rate at which work.
Reynolds Experiment Laminar Turbulent Reynolds Number
Lecture #19: Fluid Dynamics I
California State University, Chico
Introduction to Convection: Flow and Thermal Considerations
Chapter 14 Fluids Key contents Description of fluids
Lecture of : the Reynolds equations of turbulent motions JORDANIAN GERMAN WINTER ACCADMEY Prepared by: Eng. Mohammad Hamasha Jordan University of Science.
In the analysis of a tilting pad thrust bearing, the following dimensions were measured: h1 = 10 mm, h2 = 5mm, L = 10 cm, B = 24 cm The shaft rotates.
Flow and Thermal Considerations
Convection Prepared by: Nimesh Gajjar. CONVECTIVE HEAT TRANSFER Convection heat transfer involves fluid motion heat conduction The fluid motion enhances.
Introduction to Convection: Flow and Thermal Considerations
PHAROS UNIVERSITY ME 259 FLUID MECHANICS FOR ELECTRICAL STUDENTS Basic Equations for a Control Volume.
Energy Consideration in Steady Flow
Aula Teórica 18 & 19 Adimensionalização. Nº de Reynolds e Nº de Froude. Teorema dos PI’s, Diagrama de Moody, Equação de Bernoulli Generalizada e Coeficientes.
Boundary Layer Laminar Flow Re ‹ 2000 Turbulent Flow Re › 4000.
Reynolds Transport Theorem We need to relate time derivative of a property of a system to rate of change of that property within a certain region (C.V.)
Pressure distribution in a fluid Pressure and pressure gradient Lecture 4 Mecânica de Fluidos Ambiental 2015/2016.
Dr. R. Nagarajan Professor Dept of Chemical Engineering IIT Madras
Convection: Internal Flow ( )
Dr. Jason Roney Mechanical and Aerospace Engineering
1 Chapter 6 Flow Analysis Using Differential Methods ( Differential Analysis of Fluid Flow)
Aula Teórica 9&10 Equação de Evolução. Exemplos. Caso 1D.
FREE CONVECTION 7.1 Introduction Solar collectors Pipes Ducts Electronic packages Walls and windows 7.2 Features and Parameters of Free Convection (1)
Mechanical Energy Balance
OC FLOW: ENERGY CONCEPTS, CHANNEL ANALYSIS
Mecânica de Fluidos Ambiental 2015/2016
INTRODUCTION TO CONVECTION
NNPC FSTP ENGINEERS Physics Course Code: Lesson 7.

Statika Fluida Section 3. Fluid Dynamics Objectives Introduce concepts necessary to analyse fluids in motion Identify differences between Steady/unsteady.
Pratical Lecture 4 Mecânica de Fluidos Ambiental 2015/2016.
Pipe flow analysis.
Elementary Mechanics of Fluids CE 319 F Daene McKinney Energy Equation.
CONVECTION : An Activity at Solid Boundary P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Identify and Compute Gradients.
Basic equations of fluid flow. The principles of physics most useful in the applications of the fluid mechanics are mass- balance, or continuity ; the.
Momentum Equation and its Applications
Internal Flow: General Considerations. Entrance Conditions Must distinguish between entrance and fully developed regions. Hydrodynamic Effects: Assume.
Internal Incompressible
KINEMATICS 1. A nozzle is so shaped that the velocity of flow along the centre line changes linearly from 1.5 m/s to 15 m/s in a distance of m. Determine.
Viscous Flow in Pipes.
CHAPTER 6 Viscous Flow in Pipes
Heat Transfer Coefficient
Conservation of Energy/Bernoulli’s Equation
Volume 105, Issue 2, Pages (July 2013)
FLUID MECHANICS REVIEW
Internal Flow: General Considerations
Convective Heat Transfer
Fundamentals of TRANSPORT MECHANISMs
Presentation transcript:

Aula Teórica 17 Equação de Evolução da Energia Mecânica

Equação de Transporte de Energia Cinética Forma da Equação: Termo de Conversão de energia Mecânica em Energia interna (Calor)

Transport equation fo kinetic Energy Aimed rate of change: It can be obtained using other equations: Dissipation term. Conversion of mechanical energy into internal energy

How is mechanical energy dissipated? Shear stress has the same value on both sides of the surface sides. The work done is not the same because the velocity is not the same. The difference of work is the energy dissipated. In fact the work done on the side where velocity is higher is negative thus the difference between both sides is always negative. One can say that energy is dissipated wherever there is a velocity gradient and is maximum where that gradient is higher and not necessarily over a solid surface. τ τ ∆u

Injector pump The figure represents schematically the flow of air in a injector pump. The jet entrains surrounding air creating a pressure low that pumps the atmospheric air into the pipe. Assuming that the air enters intro the pipe at 5 m/s and the jet velocity is 30 m/s and that the pipes’ diameters are 20 e 40 mm: Where is the region of maximum shear stress ? If the entrance profile was exactly how is show in the figure, what would be the maximum shear stress? Draw a more realistic velocity profile and the corresponding shear stress profile. Compute the fluxes of (i) volume (ii) momentum, (iii) kinetic energy at the entrance section and in the section where the profile is fully developed. Compute the pressure at the entrance section assuming that viscous effects are negligible Compute the pressure in the section where the profile is fully developed assuming that the average shear along the wall is 0.05N/m 2 and that it is 1 m apart from the other section. Draw the stream lines that are passim by points A (axis) and B taking into attention the distances to the wall and to the center line. How thus the convective term vary along those lines? A B

Flow entering into a pipe