Lecture 5 Flusso Quasi-Mono-Dimensionale (forma
|
|
- Hilary Higgins
- 5 years ago
- Views:
Transcription
1 Lecture 5 Dimensionale forma Text: Motori Aeronautici Mar. 6, 2015 Dimensionale forma Mauro Valorani Univeristà La Sapienza 5.50
2 Agenda Dimensionale forma 1 quasi-monodimensionale
3 quasi-monodimensionale Dimensionale forma 5.52
4 Dimensionale forma Mach number definition M := v a a := γrt 1 dm 2 M 2 dx = 2 dv v dx 1 dt T dx Thermal EOS for a single species ideal gas p = ρrt ; R = R W 1 dp dt p dx 1 T dx 1 ρ Caloric EOS for a single species ideal gas dρ dx = 0 h = c pt ; dh dx = dt cp cp ; cp cv = R ; dx R = γ γ 1 ; γ = cp c v Stagnation Total enthalpy h 0 = c p = h + v 2 2 ; = T 1 + γ 1 M 2 2 dh 0 dx = d cp dx = dh dx + v dv dx = dt cp dx + v dv dx 5.53
5 Mass Steady form 0 = ρ V nda ṁ := ρ V nax = const A Dimensionale forma dṁ dx = 0 0 = 1 da A dx + 1 dv v dx + 1 dρ ρ dx ; v := V n Momentum Steady form F = S 2 V dṁ S 1 V dṁ S Sw =S 1 +S 2 p n + τ t ds G Adp + τ c dx + XAdx = ρvadv ; τ = ρ v 2 f ; X = 0 ; c := 2πR 2 dp dx + τ c = ρv dv dp A dx ; dx + τ c = γpm2 v dv A v 2 dx 1 dp p dx + τ c = γm 2 1 dv p A v dx ; τ p = ρ p f v 2 2 = γm2 v f v = γm2 2 f 1 dp p dx + γm2 2 f c = γm 2 1 dv A v dx ; F := f c A = f 2πR πr = 4 f ; D := 2R 2 D 1 p dp dx + 1 dv γm2 v dx + γm2 2 F =
6 Dimensionale forma d dx [h + 12 ] Q v 2 = ṁ Ẇ ṁ dh dx + v dv dx = dq dw ; dv c p dt dx + v v 2M 2 dm 2 dx + v 2T Q ; dq := ṁ ; dw := ṁ Ẇ dx = v dm 2 2M 2 dx + v dt 2T dx dt = dq dw dx No work exchange in duct: dw = 0 Heat exchange measured as a change in total temperature: dq = c pd c p + v 2 2T dt c p dx + v 2 2T dt dx = cp dt dx + v M2 γrt 2c pt 1 + γ 1 dt M 2 2 dx + γ 1M2 T 2 dm 2 2M 2 dx = cpd dt dx = cp 1 + γ dm 2 M 2 dx = d ; = T M 2 dt dx 1 + γ 1 M T dt dx + δm2 1 dm δm 2 M 2 dx = d ; δ := γ
7 Differential Form Dimensionale forma is a set of 5 ODEs in 5 unknowns: ρ, v, M, p, T A A + v v + ρ ρ = γf M2 + p p + γm2 v = 0 v δm 2 M 1 + δm 2 M + T T = p p T T ρ ρ = 0 2M M = T T + 2v v The processes forcing the changes of the state variables along the duct are: Variable duct shape pos/neg; the cross-section area, A = Ax, is a prescribed function of space: A pos/neg Heat by Friction sempre pos; F := f c A = f 2πR πr 2 = 4 D f x, Re,... > 0 Heat transfer pos/neg; the total temperature, = x, is a prescribed function of space: pos/neg 5.56
8 Solution Dimensionale forma Solution γm 2 p 2 A + A F p M, γ, x = 2A 1 + γ 2δM 2 ρ 2γ 2δM 2 A + A γfm ρ M, γ, x = v v M, γ, x = M M M, γ, x = T M, γ, x = 1 + 2δM δm 2 2A 1 + γ 2δM 2 2 A + A γfm δm 2 2A 1 + γ 2δM δm 2 2 A + A γfm 2 + 2A 1 + γ 2δM 2 T 2δM 2 A + A γδfm 4 + A 1 + γ 2δM δm 2 T γm γm δm 2 T 0 Remark: in general the state of the system defined by the 5 unknowns changes because of the simultaneous action of the 3 driving processes 5.57
9 Suppose of zeroing out one driving process at the time: the state of the system will change because of the individual action of one of the 3 driving processes; a table of "influence coefficients" can be constructed that reads as: M M T T Area A A γM2 1+M 2 Friction F Heat γm γM M 2 1+γM2 1+γγM 4 1+M M γM 2 p p γm2 1+M 2 v v γm 2 1+M 2 1 γm 2 1+M 2 2 2M γM 2 1+γM M γM2 1+γM 2 1+M 2 γm γM2 1+M γM2 1+M 2 All depend on Mach number M and ratio of specific heat γ, only All denominators approach zero for M 1; this condition is said to be critical because the product of the influence coefficient times the area change, friction term, or heat addition term becomes infinitely large unless A, F, or vanish as Mach tends to unity Dimensionale forma 5.58
10 Dimensionale forma General definition ds γ R = ds R = Area is isentropic Friction is irreversible Heat addition is irreversible γ dt γ 1 T dp p = M γf + γ d dp 0 γ 1 p M γ γ ds R = 0 ds R = γ 2 M2 F > 0 ds R = γ 1 + δm 2 < / > 0 γ 1 T 0 cooling/heating 5.59
11 At critical conditions M=1, and with all 3 processes active, the relative change of Mach number is zero for: M sonicflowcondition = Numerator[ ] = 0 /.{M = 1} M 2 A = A γf γ Thus, at M = 1, the 3 driving processes are not independent one to another. At critical conditions M=1, and with no friction, the relative change of Mach number is zero for: Solve [sonicflowcondition/.{f = 0}, A ] A = 1 + γa T 0 2 At critical conditions, and no friction, the area change depends on heat addition Solve [ sonicflowcondition/. { T 0 = 0}, A ] Dimensionale forma A = 1 2 γa F At critical conditions, and no heat addition, the area change depends on friction 5.60
12 If lim M 1 f M = lim M 1 gm = 0 or ± and lim M 1 f M/g M exists, then: f M lim M 1 gm = lim f M M 1 g M The differentiation of the numerator and denominator often simplifies the quotient and/or converts it to a determinate form, allowing the limit to be evaluated more easily. D[Numerator[MxM], x] 2δM M 2 A + A γf M γm δm 2 2A + A γf M γm 2 2 A +A 2γM M F + + T 0 + γm 2 F + F + D[Denominator[MxM], x] Dimensionale forma γ 2δM 2 A + 2γ 2δA M M + 2A 1 + γ 2δM
13 Dimensionale forma Area [ Only Solve M D[Numerator[MxM],x] == M /. D[Denominator[MxM],x] { T 0 = 0, T 0 = 0, F = 0, F = 0, A = 0, M = 1 }, M ] {{ } { }} 1 + γa M 1 + γa = 2, M = + A 2 A Reduce [{1 + γa > 0, γ > 1}, {A }] A > 0 Real solutions for M exist only for A >0 when A = 0 = A has a minimum throat For A >0, both positive and negative values of M are possible sub or super sonic flow depending on the downstream boundary conditions 5.62
14 Dimensionale forma [ Solve M D[Numerator[MxM],x] == M /. D[Denominator[MxM],x] { T 0 = 0, F = 0, F = 0, A = 0, A = 0, M = 1 }, M ] M = 1 + γ 2 T 0 2 2, M = + Reduce [{ 1 + γ 2 > 0, > 0, γ > 1 }, { }] > 0 && T 0 < γ 2 T Real solutions for M exist only for T 0 < 0 when T 0 = 0 = has a maximum For T 0 < 0, both positive and negative values of M are possible sub or super sonic flow depending on the downstream boundary conditions 5.63
15 Dimensionale forma [ M D[Numerator[MxM], x] Solve == /. M D[Denominator[MxM], x] { T A 0 = 0, A = 0, F = 0, F = 0, M = 1 }, M ] M = ± 1 + γ 2 A γa T A Reduce [{ 1 + γ 2 A γa } { > 0, A > 0, γ > 1, A, }] T0 A Reals && T 0 < 2 A A + γa when T 0 = 0 && A =0, real solutions for M < 2 A 1 + γ A exist only if: 5.64
16 [ M D[Numerator[MxM], x] Solve == /. M D[Denominator[MxM], x] { T A 0 = 0, A = 0, F = 0, M = 1 }, M ] Dimensionale forma M = ± 1 + γ 2 A + A γ F γt A [{ 0 Reduce 1 + γ 2T0 A + A γ F γt } 0 > 0, A > 0, γ > 1, { F, A, T }] }] 0 T0 F A Reals && T 0 < γa F + 2 A A + γa when T 0 = 0 && A =0 && F = 0, real solutions for M < γ 1 + γ F + 2 A 1 + γ A exist only if: 5.65
Section 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 information4.1 LAWS OF MECHANICS - Review
4.1 LAWS OF MECHANICS - Review Ch4 9 SYSTEM System: Moving Fluid Definitions: System is defined as an arbitrary quantity of mass of fixed identity. Surrounding is everything external to this system. Boundary
More informationGasdynamics 1-D compressible, inviscid, stationary, adiabatic flows
Gasdynamics 1-D compressible, inviscid, stationary, adiabatic flows 1st law of thermodynamics ρ const Kontrollfläche 1 2 m u 2 u 1 z Q 12 +P 12 = ṁ } h 2 h {{} 1 Enthalpy Q 12 + 1 2 (u2 2 u2 1 }{{} ) +
More informationApplied Gas Dynamics Flow With Friction and Heat Transfer
Applied Gas Dynamics Flow With Friction and Heat Transfer Ethirajan Rathakrishnan Applied Gas Dynamics, John Wiley & Sons (Asia) Pte Ltd c 2010 Ethirajan Rathakrishnan 1 / 121 Introduction So far, we have
More informationTurbomachinery & Turbulence. Lecture 2: One dimensional thermodynamics.
Turbomachinery & Turbulence. Lecture 2: One dimensional thermodynamics. F. Ravelet Laboratoire DynFluid, Arts et Metiers-ParisTech February 3, 2016 Control volume Global balance equations in open systems
More informationLecture-2. One-dimensional Compressible Fluid Flow in Variable Area
Lecture-2 One-dimensional Compressible Fluid Flow in Variable Area Summary of Results(Cont..) In isoenergetic-isentropic flow, an increase in velocity always corresponds to a Mach number increase and vice
More information2013/5/22. ( + ) ( ) = = momentum outflow rate. ( x) FPressure. 9.3 Nozzles. δ q= heat added into the fluid per unit mass
9.3 Nozzles (b) omentum conservation : (i) Governing Equations Consider: nonadiabatic ternal (body) force ists variable flow area continuously varying flows δq f ternal force per unit volume +d δffdx dx
More informationRocket Thermodynamics
Rocket Thermodynamics PROFESSOR CHRIS CHATWIN LECTURE FOR SATELLITE AND SPACE SYSTEMS MSC UNIVERSITY OF SUSSEX SCHOOL OF ENGINEERING & INFORMATICS 25 TH APRIL 2017 Thermodynamics of Chemical Rockets ΣForce
More informationIntroduction to Aerospace Engineering
Introduction to Aerospace Engineering Lecture slides Challenge the future 3-0-0 Introduction to Aerospace Engineering Aerodynamics 5 & 6 Prof. H. Bijl ir. N. Timmer Delft University of Technology 5. Compressibility
More informationCompressible Duct Flow with Friction
Compressible Duct Flow with Friction We treat only the effect of friction, neglecting area change and heat transfer. The basic assumptions are 1. Steady one-dimensional adiabatic flow 2. Perfect gas with
More informationIsentropic Duct Flows
An Internet Book on Fluid Dynamics Isentropic Duct Flows In this section we examine the behavior of isentropic flows, continuing the development of the relations in section (Bob). First it is important
More informationIntroduction to Chemical Engineering Thermodynamics. Chapter 7. KFUPM Housam Binous CHE 303
Introduction to Chemical Engineering Thermodynamics Chapter 7 1 Thermodynamics of flow is based on mass, energy and entropy balances Fluid mechanics encompasses the above balances and conservation of momentum
More informationFanno Flow. Gas Dynamics
Fanno Flow Simple frictional flow ( Fanno Flow Adiabatic frictional flow in a constant-area duct * he Flow of a compressible fluid in a duct is Always accompanied by :- ariation in the cross sectional
More informationIX. COMPRESSIBLE FLOW. ρ = P
IX. COMPRESSIBLE FLOW Compressible flow is the study of fluids flowing at speeds comparable to the local speed of sound. This occurs when fluid speeds are about 30% or more of the local acoustic velocity.
More informationWhere does Bernoulli's Equation come from?
Where does Bernoulli's Equation come from? Introduction By now, you have seen the following equation many times, using it to solve simple fluid problems. P ρ + v + gz = constant (along a streamline) This
More informationFundamentals of compressible and viscous flow analysis - Part II
Fundamentals of compressible and viscous flow analysis - Part II Lectures 3, 4, 5 Instantaneous and averaged temperature contours in a shock-boundary layer interaction. Taken from (Pasquariello et al.,
More informationTo study the motion of a perfect gas, the conservation equations of continuity
Chapter 1 Ideal Gas Flow The Navier-Stokes equations To study the motion of a perfect gas, the conservation equations of continuity ρ + (ρ v = 0, (1.1 momentum ρ D v Dt = p+ τ +ρ f m, (1.2 and energy ρ
More information5. Coupling of Chemical Kinetics & Thermodynamics
5. Coupling of Chemical Kinetics & Thermodynamics Objectives of this section: Thermodynamics: Initial and final states are considered: - Adiabatic flame temperature - Equilibrium composition of products
More informationIntroduction to Gas Dynamics All Lecture Slides
Introduction to Gas Dynamics All Lecture Slides Teknillinen Korkeakoulu / Helsinki University of Technology Autumn 009 1 Compressible flow Zeroth law of thermodynamics 3 First law of thermodynamics 4 Equation
More informationP 1 P * 1 T P * 1 T 1 T * 1. s 1 P 1
ME 131B Fluid Mechanics Solutions to Week Three Problem Session: Isentropic Flow II (1/26/98) 1. From an energy view point, (a) a nozzle is a device that converts static enthalpy into kinetic energy. (b)
More informationIntroduction to Aerospace Engineering
Introduction to Aerospace Engineering Lecture slides Challenge the future 4-0-0 Introduction to Aerospace Engineering Aerodynamics 3 & 4 Prof. H. Bijl ir. N. Timmer Delft University of Technology Challenge
More informationIntroduction to Fluid Mechanics. Chapter 13 Compressible Flow. Fox, Pritchard, & McDonald
Introduction to Fluid Mechanics Chapter 13 Compressible Flow Main Topics Basic Equations for One-Dimensional Compressible Flow Isentropic Flow of an Ideal Gas Area Variation Flow in a Constant Area Duct
More informationModeling and Analysis of Dynamic Systems
Modeling and Analysis of Dynamic Systems Dr. Guillaume Ducard Fall 2017 Institute for Dynamic Systems and Control ETH Zurich, Switzerland G. Ducard c 1 / 34 Outline 1 Lecture 7: Recall on Thermodynamics
More informationSteady waves in compressible flow
Chapter Steady waves in compressible flow. Oblique shock waves Figure. shows an oblique shock wave produced when a supersonic flow is deflected by an angle. Figure.: Flow geometry near a plane oblique
More informationAerodynamics. Basic Aerodynamics. Continuity equation (mass conserved) Some thermodynamics. Energy equation (energy conserved)
Flow with no friction (inviscid) Aerodynamics Basic Aerodynamics Continuity equation (mass conserved) Flow with friction (viscous) Momentum equation (F = ma) 1. Euler s equation 2. Bernoulli s equation
More informationHIGH SPEED GAS DYNAMICS HINCHEY
HIGH SPEED GAS DYNAMICS HINCHEY MACH WAVES Mach Number is the speed of something divided by the local speed of sound. When an infinitesimal disturbance moves at a steady speed, at each instant in time
More informationThermoacoustic Devices
Thermoacoustic Devices Peter in t panhuis Sjoerd Rienstra Han Slot 24th April 2008 Down-well power generation Vortex shedding in side branch Vortex shedding creates standing wave Porous medium near closed
More informationFluid Mechanics - Course 123 COMPRESSIBLE FLOW
Fluid Mechanics - Course 123 COMPRESSIBLE FLOW Flow of compressible fluids in a p~pe involves not only change of pressure in the downstream direction but also a change of both density of the fluid and
More informationPlease welcome for any correction or misprint in the entire manuscript and your valuable suggestions kindly mail us
Problems of Practices Of Fluid Mechanics Compressible Fluid Flow Prepared By Brij Bhooshan Asst. Professor B. S. A. College of Engg. And Technology Mathura, Uttar Pradesh, (India) Supported By: Purvi Bhooshan
More informationAOE 3114 Compressible Aerodynamics
AOE 114 Compressible Aerodynamics Primary Learning Objectives The student will be able to: 1. Identify common situations in which compressibility becomes important in internal and external aerodynamics
More informationReview of Fundamentals - Fluid Mechanics
Review of Fundamentals - Fluid Mechanics Introduction Properties of Compressible Fluid Flow Basics of One-Dimensional Gas Dynamics Nozzle Operating Characteristics Characteristics of Shock Wave A gas turbine
More informationCompressible Flow - TME085
Compressible Flow - TME085 Lecture 14 Niklas Andersson Chalmers University of Technology Department of Mechanics and Maritime Sciences Division of Fluid Mechanics Gothenburg, Sweden niklas.andersson@chalmers.se
More informationSYSTEMS VS. CONTROL VOLUMES. Control volume CV (open system): Arbitrary geometric space, surrounded by control surfaces (CS)
SYSTEMS VS. CONTROL VOLUMES System (closed system): Predefined mass m, surrounded by a system boundary Control volume CV (open system): Arbitrary geometric space, surrounded by control surfaces (CS) Many
More informationCompressible Flow - TME085
Compressible Flow - TME085 Lecture 13 Niklas Andersson Chalmers University of Technology Department of Mechanics and Maritime Sciences Division of Fluid Mechanics Gothenburg, Sweden niklas.andersson@chalmers.se
More informationAngular momentum equation
Angular momentum equation For angular momentum equation, B =H O the angular momentum vector about point O which moments are desired. Where β is The Reynolds transport equation can be written as follows:
More information4 Compressible Fluid Dynamics
4 Compressible Fluid Dynamics 4. Compressible flow definitions Compressible flow describes the behaviour of fluids that experience significant variations in density under the application of external pressures.
More informationFundamentals of Gas Dynamics (NOC16 - ME05) Assignment - 10 : Solutions
Fundamentals of Gas Dynamics (NOC16 - ME05) Assignment - 10 : Solutions Manjul Sharma & Aswathy Nair K. Department of Aerospace Engineering IIT Madras April 18, 016 (Note : The solutions discussed below
More informationSteady, 1-d, constant area, adiabatic flow with no external work but with friction Conserved quantities
School of Aerosace Engineering Stead, -d, constant area, adiabatic flow with no external work but with friction Conserved quantities since adiabatic, no work: h o constant since Aconst: mass fluxρvconstant
More informationSPECTRAL TECHNOLOGIES FOR ANALYZING 3D CONVERGING-DIVERGING NOZZLE, VENTURI TUBE, AND 90-DEGREE BEND DUCT. Undergraduate Honors Thesis
SPECTRAL TECHNOLOGIES FOR ANALYZING 3D CONVERGING-DIVERGING NOZZLE, VENTURI TUBE, AND 90-DEGREE BEND DUCT Undergraduate Honors Thesis In Partial Fulfillment of the Requirements for Graduation with Distinction
More informationvector H. If O is the point about which moments are desired, the angular moment about O is given:
The angular momentum A control volume analysis can be applied to the angular momentum, by letting B equal to angularmomentum vector H. If O is the point about which moments are desired, the angular moment
More informationThermodynamics ENGR360-MEP112 LECTURE 7
Thermodynamics ENGR360-MEP11 LECTURE 7 Thermodynamics ENGR360/MEP11 Objectives: 1. Conservation of mass principle.. Conservation of energy principle applied to control volumes (first law of thermodynamics).
More informationNotes #4a MAE 533, Fluid Mechanics
Notes #4a MAE 533, Fluid Mechanics S. H. Lam lam@princeton.edu http://www.princeton.edu/ lam October 23, 1998 1 The One-dimensional Continuity Equation The one-dimensional steady flow continuity equation
More informationII/IV B.Tech (Regular) DEGREE EXAMINATION. (1X12 = 12 Marks) Answer ONE question from each unit.
Page 1 of 8 Hall Ticket Number: 14CH 404 II/IV B.Tech (Regular) DEGREE EXAMINATION June, 2016 Chemical Engineering Fourth Semester Engineering Thermodynamics Time: Three Hours Maximum : 60 Marks Answer
More informationShock and Expansion Waves
Chapter For the solution of the Euler equations to represent adequately a given large-reynolds-number flow, we need to consider in general the existence of discontinuity surfaces, across which the fluid
More informationDishwasher. Heater. Homework Solutions ME Thermodynamics I Spring HW-1 (25 points)
HW-1 (25 points) (a) Given: 1 for writing given, find, EFD, etc., Schematic of a household piping system Find: Identify system and location on the system boundary where the system interacts with the environment
More informationNotes #6 MAE 533, Fluid Mechanics
Notes #6 MAE 533, Fluid Mechanics S. H. Lam lam@princeton.edu http://www.princeton.edu/ lam October 1, 1998 1 Different Ways of Representing T The speed of sound, a, is formally defined as ( p/ ρ) s. It
More informationA Study of Transonic Flow and Airfoils. Presented by: Huiliang Lui 30 th April 2007
A Study of Transonic Flow and Airfoils Presented by: Huiliang Lui 3 th April 7 Contents Background Aims Theory Conservation Laws Irrotational Flow Self-Similarity Characteristics Numerical Modeling Conclusion
More informationReview of First and Second Law of Thermodynamics
Review of First and Second Law of Thermodynamics Reading Problems 4-1 4-4 4-32, 4-36, 4-87, 4-246 5-2 5-4, 5.7 6-1 6-13 6-122, 6-127, 6-130 Definitions SYSTEM: any specified collection of matter under
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 informationAME 436. Energy and Propulsion. Lecture 15 Propulsion 5: Hypersonic propulsion
AME 436 Energy and Propulsion Lecture 5 Propulsion 5: Hypersonic propulsion Outline!!!!!! Why hypersonic propulsion? What's different about it? Conventional ramjet heat addition at M
More informationAerothermodynamics of high speed flows
Aerothermodynamics of high speed flows AERO 0033 1 Lecture 6: D potential flow, method of characteristics Thierry Magin, Greg Dimitriadis, and Johan Boutet Thierry.Magin@vki.ac.be Aeronautics and Aerospace
More informationVarious lecture notes for
Various lecture notes for 18311. R. R. Rosales (MIT, Math. Dept., 2-337) April 12, 2013 Abstract Notes, both complete and/or incomplete, for MIT s 18.311 (Principles of Applied Mathematics). These notes
More informationContinuum Mechanics Lecture 5 Ideal fluids
Continuum Mechanics Lecture 5 Ideal fluids Prof. http://www.itp.uzh.ch/~teyssier Outline - Helmholtz decomposition - Divergence and curl theorem - Kelvin s circulation theorem - The vorticity equation
More informationTutorial Materials for ME 131B Fluid Mechanics (Compressible Flow & Turbomachinery) Calvin Lui Department of Mechanical Engineering Stanford University Stanford, CA 94305 March 1998 Acknowledgments This
More informationModule-5: Hypersonic Boundary Layer theory. Lecture-20: Hypersonic boundary equation
Module-5: Hypersonic Boundary Layer theory Lecture-0: Hypersonic boundary equation 0.1 Governing Equations for Viscous Flows The Navier-Stokes (NS) equaadtions are the governing equations for the viscous
More informationChapter 17. For the most part, we have limited our consideration so COMPRESSIBLE FLOW. Objectives
Chapter 17 COMPRESSIBLE FLOW For the most part, we have limited our consideration so far to flows for which density variations and thus compressibility effects are negligible. In this chapter we lift this
More informationCHAPTER (2) FLUID PROPERTIES SUMMARY DR. MUNZER EBAID MECH.ENG.DEPT.
CHAPTER () SUMMARY DR. MUNZER EBAID MECH.ENG.DEPT. 08/1/010 DR.MUNZER EBAID 1 System Is defined as a given quantity of matter. Extensive Property Can be identified when it is Dependent on the total mass
More information(S1.3) dt Taking into account equation (S1.1) and the fact that the reaction volume is constant, equation (S1.3) can be rewritten as:
roblem 1 Overall Material alance: dn d( ρv) dv dρ = =ρifi ρf ρ + V =ρifi ρ F (S1.1) ssuming constant density and reactor volume, equation (S1.1) yields: ( ) ρ F F = 0 F F = 0 (S1.2) i i Therefore, the
More informationUnsteady Emptying of a Pressure Vessel
Mechanics and Mechanical Engineering Vol. 7, No. 2 (2004) 121 125 c Technical University of Lodz Unsteady Emptying of a Pressure Vessel Bedier B. EL-NAGGAR and Ismail A. KHOLEIF Department of Engineering,
More informationExercise Set 4. D s n ds + + V. s dv = V. After using Stokes theorem, the surface integral becomes
Exercise Set Exercise - (a) Let s consider a test volum in the pellet. The substract enters the pellet by diffusion and some is created and disappears due to the chemical reaction. The two contribute to
More informationThermodynamics revisited
Thermodynamics revisited How can I do an energy balance for a reactor system? 1 st law of thermodynamics (differential form): de de = = dq dq--dw dw Energy: de = du + de kin + de pot + de other du = Work:
More informationChemistry. Lecture 10 Maxwell Relations. NC State University
Chemistry Lecture 10 Maxwell Relations NC State University Thermodynamic state functions expressed in differential form We have seen that the internal energy is conserved and depends on mechanical (dw)
More informationPART 0 PRELUDE: REVIEW OF "UNIFIED ENGINEERING THERMODYNAMICS"
PART 0 PRELUDE: REVIEW OF "UNIFIED ENGINEERING THERMODYNAMICS" PART 0 - PRELUDE: REVIEW OF UNIFIED ENGINEERING THERMODYNAMICS [IAW pp -, 3-41 (see IAW for detailed SB&VW references); VN Chapter 1] 01 What
More information6.1 Propellor e ciency
Chapter 6 The Turboprop cycle 6. Propellor e ciency The turboprop cycle can be regarded as a very high bypass limit of a turbofan. Recall that the propulsive e ciency of a thruster with P e = P 0 and f
More informationLeaving Cert Differentiation
Leaving Cert Differentiation Types of Differentiation 1. From First Principles 2. Using the Rules From First Principles You will be told when to use this, the question will say differentiate with respect
More informationChapter 5: Mass, Bernoulli, and Energy Equations
Chapter 5: Mass, Bernoulli, and Energy Equations Introduction This chapter deals with 3 equations commonly used in fluid mechanics The mass equation is an expression of the conservation of mass principle.
More informationModeling and Analysis of Dynamic Systems
Modeling and Analysis of Dynamic Systems Dr. Guillaume Ducard Fall 2017 Institute for Dynamic Systems and Control ETH Zurich, Switzerland G. Ducard c 1 / 21 Outline 1 Lecture 4: Modeling Tools for Mechanical
More informationIn this lecture... Centrifugal compressors Thermodynamics of centrifugal compressors Components of a centrifugal compressor
Lect- 3 In this lecture... Centrifugal compressors Thermodynamics of centrifugal compressors Components of a centrifugal compressor Centrifugal compressors Centrifugal compressors were used in the first
More informationDistinguish between. and non-thermal energy sources.
Distinguish between System & Surroundings We also distinguish between thermal We also distinguish between thermal and non-thermal energy sources. P Work The gas in the cylinder is the system How much work
More informationAA214B: NUMERICAL METHODS FOR COMPRESSIBLE FLOWS
AA214B: NUMERICAL METHODS FOR COMPRESSIBLE FLOWS 1 / 29 AA214B: NUMERICAL METHODS FOR COMPRESSIBLE FLOWS Hierarchy of Mathematical Models 1 / 29 AA214B: NUMERICAL METHODS FOR COMPRESSIBLE FLOWS 2 / 29
More informationThe conservation equations
Chapter 5 The conservation equations 5.1 Leibniz rule for di erentiation of integrals 5.1.1 Di erentiation under the integral sign According to the fundamental theorem of calculus if f is a smooth function
More informationChemical Reaction Engineering
Lecture 21 Chemical Reaction Engineering (CRE) is the field that studies the rates and mechanisms of chemical reactions and the design of the reactors in which they take place. Web Lecture 21 Class Lecture
More informationDetailed Derivation of Fanno Flow Relationships
Detailed Derivation of Fanno Flow Relationships Matthew MacLean, Ph.D. Version. October 03 v. fixed a sign error on Eq. 5 ! My motivation for writing this note results from preparing course notes for the
More informationThe Virial Theorem for Stars
The Virial Theorem for Stars Stars are excellent examples of systems in virial equilibrium. To see this, let us make two assumptions: 1) Stars are in hydrostatic equilibrium 2) Stars are made up of ideal
More informationOE4625 Dredge Pumps and Slurry Transport. Vaclav Matousek October 13, 2004
OE465 Vaclav Matousek October 13, 004 1 Dredge Vermelding Pumps onderdeel and Slurry organisatie Transport OE465 Vaclav Matousek October 13, 004 Dredge Vermelding Pumps onderdeel and Slurry organisatie
More informationRichard Nakka's Experimental Rocketry Web Site
Página 1 de 7 Richard Nakka's Experimental Rocketry Web Site Solid Rocket Motor Theory -- Nozzle Theory Nozzle Theory The rocket nozzle can surely be described as the epitome of elegant simplicity. The
More informationChapter Two. Basic Thermodynamics, Fluid Mechanics: Definitions of Efficiency. Laith Batarseh
Chapter Two Basic Thermodynamics, Fluid Mechanics: Definitions of Efficiency Laith Batarseh The equation of continuity Most analyses in this book are limited to one-dimensional steady flows where the velocity
More informationME Thermodynamics I
Homework - Week 01 HW-01 (25 points) Given: 5 Schematic of the solar cell/solar panel Find: 5 Identify the system and the heat/work interactions associated with it. Show the direction of the interactions.
More informationDrag of a thin wing and optimal shape to minimize it
Drag of a thin wing and optimal shape to minimize it Alejandro Pozo December 21 st, 211 Outline 1 Statement of the problem 2 Inviscid compressible flows 3 Drag for supersonic case 4 Example of optimal
More informationThe underlying prerequisite to the application of thermodynamic principles to natural systems is that the system under consideration should be at equilibrium. http://eps.mcgill.ca/~courses/c220/ Reversible
More informationME19b. FINAL REVIEW SOLUTIONS. Mar. 11, 2010.
ME19b. FINAL REVIEW SOLTIONS. Mar. 11, 21. EXAMPLE PROBLEM 1 A laboratory wind tunnel has a square test section with side length L. Boundary-layer velocity profiles are measured at two cross-sections and
More informationA SHORT INTRODUCTION TO TWO-PHASE FLOWS Two-phase flows balance equations
A SHORT INTRODUCTION TO TWO-PHASE FLOWS Two-phase flows balance equations Hervé Lemonnier DM2S/STMF/LIEFT, CEA/Grenoble, 38054 Grenoble Cedex 9 Ph. +33(0)4 38 78 45 40 herve.lemonnier@cea.fr, herve.lemonnier.sci.free.fr/tpf/tpf.htm
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 informationLecture 4. Differential Analysis of Fluid Flow Navier-Stockes equation
Lecture 4 Differential Analysis of Fluid Flow Navier-Stockes equation Newton second law and conservation of momentum & momentum-of-momentum A jet of fluid deflected by an object puts a force on the object.
More informationPROCESS SYSTEMS ENGINEERING Dr.-Ing. Richard Hanke-Rauschenbach
Otto-von-Guerice University Magdeburg PROCESS SYSTEMS ENGINEERING Dr.-Ing. Richard Hane-Rauschenbach Project wor No. 1, Winter term 2011/2012 Sample Solution Delivery of the project handout: Wednesday,
More informationLecture with Numerical Examples of Ramjet, Pulsejet and Scramjet
Lecture 41 1 Lecture with Numerical Examples of Ramjet, Pulsejet and Scramjet 2 Problem-1 Ramjet A ramjet is flying at Mach 1.818 at an altitude 16.750 km altitude (Pa = 9.122 kpa, Ta= - 56.5 0 C = 216.5
More informationThe forced response of choked nozzles and supersonic diffusers
J. Fluid Mech. (27), vol. 585, pp. 28 34. c 27 Cambridge University Press doi:.7/s22276647 Printed in the United Kingdom 28 The forced response of choked nozzles and supersonic diffusers WILLIAM H. MOASE,
More informationWhy integrate? 1 Introduction. 2 Integrating constant functions
Why integrate? 1 Introduction Teaching physics my colleagues and I often find that some of you find it difficult to see when you need to use integration. This session will explain the need for integration
More informationEntropy and the Second Law of Thermodynamics
Entropy and the Second Law of hermodynamics Reading Problems 6-, 6-2, 6-7, 6-8, 6-6-8, 6-87, 7-7-0, 7-2, 7-3 7-39, 7-46, 7-6, 7-89, 7-, 7-22, 7-24, 7-30, 7-55, 7-58 Why do we need another law in thermodynamics?
More informationIsentropic Efficiency in Engineering Thermodynamics
June 21, 2010 Isentropic Efficiency in Engineering Thermodynamics Introduction This article is a summary of selected parts of chapters 4, 5 and 6 in the textbook by Moran and Shapiro (2008. The intent
More informationdf da df = force on one side of da due to pressure
I. Review of Fundamental Fluid Mechanics and Thermodynamics 1. 1 Some fundamental aerodynamic variables htt://en.wikiedia.org/wiki/hurricane_ivan_(2004) 1) Pressure: the normal force er unit area exerted
More informationSummary of the Equations of Fluid Dynamics
Reference: Summary of the Equations of Fluid Dynamics Fluid Mechanics, L.D. Landau & E.M. Lifshitz 1 Introduction Emission processes give us diagnostics with which to estimate important parameters, such
More informationModule 2 : Lecture 1 GOVERNING EQUATIONS OF FLUID MOTION (Fundamental Aspects)
Module : Lecture 1 GOVERNING EQUATIONS OF FLUID MOTION (Fundamental Aspects) Descriptions of Fluid Motion A fluid is composed of different particles for which the properties may change with respect to
More informationEng Thermodynamics I conservation of mass; 2. conservation of energy (1st Law of Thermodynamics); and 3. the 2nd Law of Thermodynamics.
Eng3901 - Thermodynamics I 1 1 Introduction 1.1 Thermodynamics Thermodynamics is the study of the relationships between heat transfer, work interactions, kinetic and potential energies, and the properties
More informationIntroduction. Statistical physics: microscopic foundation of thermodynamics degrees of freedom 2 3 state variables!
Introduction Thermodynamics: phenomenological description of equilibrium bulk properties of matter in terms of only a few state variables and thermodynamical laws. Statistical physics: microscopic foundation
More informationMATTER TRANSPORT (CONTINUED)
MATTER TRANSPORT (CONTINUED) There seem to be two ways to identify the effort variable for mass flow gradient of the energy function with respect to mass is matter potential, µ (molar) specific Gibbs free
More informationM3/4A16. GEOMETRICAL MECHANICS, Part 1
M3/4A16 GEOMETRICAL MECHANICS, Part 1 (2009) Page 1 of 5 UNIVERSITY OF LONDON Course: M3/4A16 Setter: Holm Checker: Gibbons Editor: Chen External: Date: January 27, 2008 BSc and MSci EXAMINATIONS (MATHEMATICS)
More informationTHERMODYNAMIC ANALYSIS OF COMBUSTION PROCESSES FOR PROPULSION SYSTEMS
2nd AIAA Aerospace Sciences Paper 2-33 Meeting and Exhibit January -8, 2, Reno, NV THERMODYNAMIC ANALYSIS OF COMBUSTION PROCESSES FOR PROPULSION SYSTEMS E. Wintenberger and J. E. Shepherd Graduate Aeronautical
More information1 One-dimensional analysis
One-dimensional analysis. Introduction The simplest models for gas liquid flow systems are ones for which the velocity is uniform over a cross-section and unidirectional. This includes flows in a long
More informationE = K + U. p mv. p i = p f. F dt = p. J t 1. a r = v2. F c = m v2. s = rθ. a t = rα. r 2 dm i. m i r 2 i. I ring = MR 2.
v = v i + at x = x i + v i t + 1 2 at2 E = K + U p mv p i = p f L r p = Iω τ r F = rf sin θ v 2 = v 2 i + 2a x F = ma = dp dt = U v dx dt a dv dt = d2 x dt 2 A circle = πr 2 A sphere = 4πr 2 V sphere =
More information