Isentropic and Ideal Gas Density Relationships

Similar documents
High Speed Aerodynamics Prof. K. P. Sinhamahapatra Department of Aerospace Engineering Indian Institute of Technology, Kharagpur

CO MPa (abs) 20 C

Differential Relations for Fluid Flow. Acceleration field of a fluid. The differential equation of mass conservation

CFD Analysis of Supersonic Exhaust Diffuser System for Higher Altitude Simulation

Chapter 17. For the most part, we have limited our consideration so COMPRESSIBLE FLOW. Objectives

Chapter 10. Flow Rate. Flow Rate. Flow Measurements. The velocity of the flow is described at any

Lecture 6 - Boundary Conditions. Applied Computational Fluid Dynamics

du u U 0 U dy y b 0 b

TWO-DIMENSIONAL FINITE ELEMENT ANALYSIS OF FORCED CONVECTION FLOW AND HEAT TRANSFER IN A LAMINAR CHANNEL FLOW

Turbulence Modeling in CFD Simulation of Intake Manifold for a 4 Cylinder Engine

INTRODUCTION TO FLUID MECHANICS

APPLIED THERMODYNAMICS TUTORIAL 1 REVISION OF ISENTROPIC EFFICIENCY ADVANCED STEAM CYCLES

AOE 3104 Aircraft Performance Problem Sheet 2 (ans) Find the Pressure ratio in a constant temperature atmosphere:

HEAT TRANSFER ANALYSIS IN A 3D SQUARE CHANNEL LAMINAR FLOW WITH USING BAFFLES 1 Vikram Bishnoi

Diesel Cycle Analysis

Sound. References: L.D. Landau & E.M. Lifshitz: Fluid Mechanics, Chapter VIII F. Shu: The Physics of Astrophysics, Vol. 2, Gas Dynamics, Chapter 8

Modelling and Simulation of Supersonic Nozzle Using Computational Fluid Dynamics

Exergy Analysis of a Water Heat Storage Tank

Heat Transfer Prof. Dr. Ale Kumar Ghosal Department of Chemical Engineering Indian Institute of Technology, Guwahati

CFD Analysis of Swept and Leaned Transonic Compressor Rotor

Fundamentals of Fluid Mechanics

O.F.Wind Wind Site Assessment Simulation in complex terrain based on OpenFOAM. Darmstadt,

Science Insights: An International Journal

Swissmetro travels at high speeds through a tunnel at low pressure. It will therefore undergo friction that can be due to:

Distinguished Professor George Washington University. Graw Hill

Dynamic Process Modeling. Process Dynamics and Control

- momentum conservation equation ρ = ρf. These are equivalent to four scalar equations with four unknowns: - pressure p - velocity components

INLET AND EXAUST NOZZLES Chap. 10 AIAA AIRCRAFT ENGINE DESIGN R01-07/11/2011

Basic Equations, Boundary Conditions and Dimensionless Parameters

Fluid Mechanics Prof. S. K. Som Department of Mechanical Engineering Indian Institute of Technology, Kharagpur

A MTR FUEL ELEMENT FLOW DISTRIBUTION MEASUREMENT PRELIMINARY RESULTS

Theory of turbo machinery / Turbomaskinernas teori. Chapter 4

Textbook: Introduction to Fluid Mechanics by Philip J. Pritchard. John Wiley & Sons, 8th Edition, ISBN ,

Sheet 5:Chapter 5 5 1C Name four physical quantities that are conserved and two quantities that are not conserved during a process.

Chapter 8: Flow in Pipes

Air Flow Optimization via a Venturi Type Air Restrictor

ME 239: Rocket Propulsion. Over- and Under-expanded Nozzles and Nozzle Configurations. J. M. Meyers, PhD

Introduction to COMSOL. The Navier-Stokes Equations

Abaqus/CFD Sample Problems. Abaqus 6.10

Head Loss in Pipe Flow ME 123: Mechanical Engineering Laboratory II: Fluids

When the fluid velocity is zero, called the hydrostatic condition, the pressure variation is due only to the weight of the fluid.

APPLIED THERMODYNAMICS. TUTORIAL No.3 GAS TURBINE POWER CYCLES. Revise gas expansions in turbines. Study the Joule cycle with friction.

Chapter 5 MASS, BERNOULLI AND ENERGY EQUATIONS

ME6130 An introduction to CFD 1-1

Heat Transfer by Free Convection

FUNDAMENTALS OF ENGINEERING THERMODYNAMICS

INTERNATIONAL JOURNAL OF RESEARCH IN AERONAUTICAL AND MECHANICAL ENGINEERING

A LAMINAR FLOW ELEMENT WITH A LINEAR PRESSURE DROP VERSUS VOLUMETRIC FLOW ASME Fluids Engineering Division Summer Meeting

1 Foundations of Pyrodynamics

This tutorial provides a recipe for simulating L

Express Introductory Training in ANSYS Fluent Lecture 1 Introduction to the CFD Methodology

COMPUTATIONAL FLUID DYNAMICS (CFD) ANALYSIS OF INTERMEDIATE PRESSURE STEAM TURBINE

Dimensional analysis is a method for reducing the number and complexity of experimental variables that affect a given physical phenomena.

CHAPTER 4 CFD ANALYSIS OF THE MIXER

Introduction to CFD Analysis

Gas Dynamics Prof. T. M. Muruganandam Department of Aerospace Engineering Indian Institute of Technology, Madras. Module No - 12 Lecture No - 25

Averaging Pitot Tubes; Fact and Fiction

Dr.A.K.Shaik Dawood. N.V.Kamalesh. Department of Mechanical Engineering, Associate Professor, Karpagam University, Coimbatore , India.

FLOW MEASUREMENT 2001 INTERNATIONAL CONFERENCE DERIVATION OF AN EXPANSIBILITY FACTOR FOR THE V-CONE METER

Numerical Analysis of Independent Wire Strand Core (IWSC) Wire Rope

Lecture 4 Classification of Flows. Applied Computational Fluid Dynamics

Laminar Flow and Heat Transfer of Herschel-Bulkley Fluids in a Rectangular Duct; Finite-Element Analysis

Battery Thermal Management System Design Modeling

Customer Training Material. Lecture 2. Introduction to. Methodology ANSYS FLUENT. ANSYS, Inc. Proprietary 2010 ANSYS, Inc. All rights reserved.

A Comparison of Analytical and Finite Element Solutions for Laminar Flow Conditions Near Gaussian Constrictions

NUMERICAL ANALYSIS OF THE EFFECTS OF WIND ON BUILDING STRUCTURES

The Use of Control Valve Sizing Equations with Simulation Based Process Data

Mohan Chandrasekharan #1

CFD Analysis of a butterfly valve in a compressible fluid

A CODE VERIFICATION EXERCISE FOR THE UNSTRUCTURED FINITE-VOLUME CFD SOLVER ISIS-CFD

a) Use the following equation from the lecture notes: = ( J K 1 mol 1) ( ) 10 L

Nozzle Vent: A Simpler Approach to Laptop Cooling

Introduction to CFD Analysis

Air Flow Measurements

Chapter 8 Maxwell relations and measurable properties

Michael Montgomery Marketing Product Manager Rosemount Inc. Russ Evans Manager of Engineering and Design Rosemount Inc.

1. Define the System SDV BDV SDV SDV SDV BDV SDV SDV SDV SDV SDV SDV. Process System TO FLARE TO FLARE BDV TO FLARE

Ravi Kumar Singh*, K. B. Sahu**, Thakur Debasis Mishra***

NUMERICAL ANALYSIS OF AERO-SPIKE NOZZLE FOR SPIKE LENGTH OPTIMIZATION

Vacuum Technology. Kinetic Theory of Gas. Dr. Philip D. Rack

Lesson. 11 Vapour Compression Refrigeration Systems: Performance Aspects And Cycle Modifications. Version 1 ME, IIT Kharagpur 1

CFD ANALAYSIS OF FLOW THROUGH A CONICAL EXHAUST DIFFUSER

Keywords: Heat transfer enhancement; staggered arrangement; Triangular Prism, Reynolds Number. 1. Introduction

Navier-Stokes Equation Solved in Comsol 4.1. Copyright Bruce A. Finlayson, 2010 See also Introduction to Chemical Engineering Computing, Wiley (2006).

HEAT TRANSFER AUGMENTATION THROUGH DIFFERENT PASSIVE INTENSIFIER METHODS

CFD SIMULATION OF SDHW STORAGE TANK WITH AND WITHOUT HEATER

AN EFFECT OF GRID QUALITY ON THE RESULTS OF NUMERICAL SIMULATIONS OF THE FLUID FLOW FIELD IN AN AGITATED VESSEL

FREESTUDY HEAT TRANSFER TUTORIAL 3 ADVANCED STUDIES

Engineering Problem Solving as Model Building

Cylinder Pressure in a Spark-Ignition Engine: A Computational Model

Isentropic flow. Wikepedia

FEASIBILITY OF A BRAYTON CYCLE AUTOMOTIVE AIR CONDITIONING SYSTEM

Adaptation of General Purpose CFD Code for Fusion MHD Applications*

1 The basic equations of fluid dynamics

CFD software overview comparison, limitations and user interfaces

Chapter 28 Fluid Dynamics

Chapter 13 OPEN-CHANNEL FLOW

Understanding Plastics Engineering Calculations

Transcription:

Isentropic and Ideal Gas Density Relationships Consider the subsonic flow of a real gas through a smooth duct with a contraction and expansion forming a gradually converging and diverging nozzle. An idealization of this type of flow is to assume that the flow is isentropic. i.e. entropy remains constant throughout, and that the gas is an ideal gas. It is a common practice to assume isentropic flow when friction effects are small, there is negligible heat transfer and there are no shocks. Since the flow is reversible and adiabatic, both the stagnation pressure and stagnation temperature are constant. For an ideal gas, an isentropic flow obeys the equation where γ is the ratio of C P, the specific heat at constant pressure, to C V, the specific heat at constant volume; P is the pressure; and Ï is the density. The subscript t stands for the total (or stagnation) conditions. In the following example, AcuSolve TM is used to solve for the isentropic flow of air in a converging diverging nozzle. The geometry is shown in Figure 1. The nozzle has constant and equal diameter inlet and outlet sections, commonly referred to as reservoir and receiver sections. Since we are neglecting viscous effects, the solution is obtained by setting the dynamic viscosity to a negligible value (practically zero) and slip boundary condition at the wall. The velocity at the inlet is 50 m/sec and pressure at the outlet is prescribed as atmospheric (P atm = 101325 Pa). For the geometry chosen, the peak Mach number reached in the throat is M â ˆ 0.63. Figure 1. Nozzle geometry

Two different cases are solved based on the treatment of the equation of state for air. Case 1. Isentropic flow is "assumed". Hence, the pressure and density are strict functions of each other. The energy equation is not solved in this case. Case 2. The ideal gas equation of state is used along with the energy equation, hence density is taken as a function of pressure and temperature using the following equation where R = C P C V is the gas constant and T is the temperature. All calculations were performed using a three dimensional tetrahedral mesh with 134492 elements and 26274 nodes. Case 1 required 17 time steps for convergence while Case 2 required 35 time steps to reach convergence. In both cases, convergence is defined to be reached when the normalized residuals for all variables are 1e 5 or less. Due to the energy conservation equation the total number of time steps to reach convergence was higher for Case 2. Figure 2 shows the convergence histories for the mass and momentum residuals for both Case 1 and 2. The solution histories for Case 2 are similar for mass and momentum residuals.

Figure 2. Normalized residuals vs. time step The conservation of mass principle tells us that the mass flow rate ( ) through a tube remains constant. Also, for the solutions obtained here, the velocity profile across the nozzle is nearly uniform so the predicted flow is nearly one dimensional. The mass flux (G) or mass flow rate per unit area varies inversely with the cross sectional area. For a given we can calculate the average G from the local cross sectional area (A C ). Figure 3 plots the average mass flux over the cross section for the solutions of Case 1 and Case 2 as a function of axial position along the nozzle. For comparison, the mass flux calculated using the classical relationship for one dimensional isentropic flow in a duct is also plotted [1].

Figure 3. Average mass flux vs axial position The Mach number (M) is the ratio of speed of the flow (u) to the speed of sound (c). The speed of sound depends on the density (Ï ), the pressure (P), the temperature (T) and the ratio of specific heats (γ) Hence, we can write

And the theoretical Mach number can be calculated from the mass flux, using the relationship The Mach numbers for both the numerical solutions along with the one dimensional flow solution are plotted in Figure 4 as a function of axial position along the nozzle. The AcuSolve TM solutions are again quite similar to each other and to the classical flow solution. Figure 4. Average Mach number vs axial position This exercise shows that good agreement is achieved between the two solutions of isentropic flow in a duct using AcuSolve TM, one using the isentropic density relationship and a second solving the energy equation and using ideal gas density relationship. Both of these solutions compare well with the classical one dimensional solution for compressible flow in a duct. This suggests that AcuSolve TM can be used to provide accurate solutions for density variation using isentropic and ideal gas relationships. [1] See, for example, Asher H. Shapiro, Compressible Fluid Flow, Ronald Press, NY, 1953.