LAMINAR FLOW (Reynolds < 2320, parabolic velocity profile) Name symbol formula unit gravity g L L
|
|
- Noel Watson
- 5 years ago
- Views:
Transcription
1 file: Fluid Flow Calculator equations 14.pdf fro: Mark van Dijk revision: DEC 01 LAMINAR FLOW (Reynolds < 30, parabolic velocity profile) Nae sybol forula unit gravity g pipe length L elevation change h inner diaeter Di distance to pipe centre r pipe crosstional area A A = 0. 5 π Di average velocity v v = flow / A Reynolds Re ρ v Di Re = η equivalent length Leq L L Leq = Di fro tables Di ( ) Di friction factor F 64 / Re relative roughness surface k/di not applicable for lainar flow friction of pipe Kw(pipe) Kw( pipe) = F L / Di friction of appendages Kw(app) Kw( app) = F Leq / Di pipe volue V V = A L litre average residence tie in pipe, transportation lag, t t = L / v = V / flow distance/velocity lag power loss in fluid P P = p flow pressure drop pipe p = g h +??? p ρ bar dynaic viscosity η Also called Newtonian shear viscosity. average shear rate γ η = τ / γ σ v v = = η x Di 4 γ (see Figure 1) N = Watt Pa.s = centipoise (estiated shear rate in round pipes) shear stress σ or τ σ = F / A N / velocity profile, v(r) V position Vposition = v (1 ( r /(0.5 Di)) ) = position r residence tie profile, t(r) = residence position r t position t position = L / Vposition shear rate profile, γ (r) γ position 4 v r γ position = 1 = shear position r (0.5 Di) 1 1
2 Figure 1: Lainar shear field due to applied shear stress. Figure : Velocity profile and shear rate profile in lainar flow. The highest shear rate is where the velocity gradient is the highest: at the wall of the pipe.
3 revision: JAN 006 LAMINAR FLOW POWERLAW FLUIDS (Reynolds < 30, parabolic velocity profile) nae sybol forula unit Gravity g pipe length L elevation change h inner diaeter Di distance to pipe centre r pipe crosstional area A A = 0. 5 π Di average velocity v v = flow / A Reynolds powerlaw Re n n 1 ρ v Di 4n Di Re = * * K 3n + 1 8v equivalent length Leq L L Leq = Di fro tables Di ( ) Di friction factor F 64 / Re relative roughness surface k/di not applicable for lainar flow friction of pipe Kw(pipe) Kw( pipe) = F L / Di friction of appendages Kw(app) Kw( app) = F Leq / Di pipe volue V V = A L litre t t = L / v = V / flow average residence tie in pipe, transportation lag, distance/velocity lag power loss in fluid P P = p flow pressure drop pipe p ρ ( ( ) ( )) 1 p = g h + Kw pipe + Kw app ρ v dynaic viscosity η Also called Newtonian shear viscosity. average shear rate γ η = τ / γ σ v v = = η x Di 4 γ (see Figure 1) bar N = Watt Pa.s = centipoise (estiated shear rate in round pipes) shear stress σ or τ σ = F / A N / velocity profile, v(r) V position ( n+ 1) / n = position r 3n + 1 r Vpos = v 1 n Di residence tie profile, t(r) = residence position r t position t position = L / Vposition shear rate profile, γ (r) γ position 4 v r γ position = = shear position r (0.5 Di) 1 NB. The highest shear rate is where the velocity gradient is the highest: at the wall of the pipe. 3
4 TURBULENT FLOW (Reynolds >= 30, flat velocity profile) nae sybol forula unit gravity g pipe length L elevation change h surface roughness k inner diaeter Di distance to pipe centre r pipe crosstional area A A = 0. 5 π Di average velocity v v = flow / A Reynolds Re ρ v Di Re = η Equivalent length Leq L L Leq = Di fro tables Di ( ) Di friction factor F = f = λ (iterative algorith of k. 5 λ = log + ColebrookWhite) 37. Di Re λ relative roughness surface k/di k / Di friction of pipe Kw(pipe) Kw( pipe) = F L / Di friction of appendages Kw(app) Kw( app) = F Leq / Di pipe volue V V = A L litre average residence tie in pipe, transportation lag, distance/velocity lag t t = L / v = V / flow power loss in fluid P N P = p flow = Watt pressure drop pipe p 1 p = ρ g h + ( Kw( pipe) + Kw( app) ) ρ v bar velocity profile, v(r) V position 1/ n Vposition = v (1 ( r /(0.5 Di)) = position r n is a function of the Reynolds nuber. Varies fro about 6 to 10. Specific values: n=7 for Re=10^5, n=9 for Re=10^6 residence tie profile, t(r) = residence position r t position t position = t = L / v = V / flow The residence tie at position r is the sae as the average residence tie. The assuption ade is that the fluid is ideally ixed due to the turbulence. 4
5 shear rate profile, γ (r) = shear position r r 0.5 Di γ position = v ( ) 6 The integral over V position. In reality the shear rate will be higher due to turbulence. γ position 5/ 6 1 average shear rate γ σ v 4 v γ = = (see Figure 1) η x Di The assuption ade is that the turbulent fluid iniu shear rate is the sae as the average shear rate for lainar flow. In reality the shear rate will be higher due to turbulence. 1 In fact it is the integral over γ position Friction factor: The chart above shows the relationship between Reynold s nuber and pipe friction. Calculation of friction factors is dependant on the type of flow that will be encountered. For Re nubers <30 the fluid flow is lainar, when Re nuber is >= 30 the fluid flow is turbulent. Lainar flow (Re < 30) : f = 64/Re Turbulent flow (Re > 30) k.5 : f = λ = log Di Re λ In case of turbulent flow, the inner roughness of the pipe work can have a significant effect on the friction factor. See also: 5
6 Figure 3: Flow disturbance of a fluid passing a cylindrical obstacle. The flow changes fro lainar to turbulent. 6
7 Tables EQUIVALENT PIPE LENGTH OF FITTINGS Bends / Tees 180 bend, R=5D [ 8 L/Di ] 90 bend, R=5D [ 16 L/Di ] 90 bend (square, R=1.5D) [ 0 L/Di ] 45 bend (square, R=1.5D) [ 16 L/Di ] Tee (flow straight through) [ 0 L/Di ] Tee (flow through side outlet) [ 65 L/Di ] Valves Gate valve open [ 13 L/Di ] ¼closed [ 39 L/Di ] ½closed [ 195 L/Di ] ¾closed [ 300 L/Di ] Mebrane valve [ 00 L/Di ] Ball valve (spherical plug valve) [ 18 L/Di ] Needle valve [ 1000 L/Di ] Butterfly valve (larger then 6 inch) [ 0 L/Di ] Globe valve [ 300 L/Di ] Nozzle (suction nozzle on vessel) [ 3 L/Di ] Check valve (inline ball type) [ 150 L/Di ] Check valve (swing type) [ 135 L/Di ] Filter (Ytype and bucket type) [ 50 L/Di ] Surface roughness value [E] Various aterials Glass Lead Copper Brass Concrete tube Steel Pipe New After longer use Slightly rusted Very rusted Galvanised Cast iron New With bituen layer Slightly rusted Very rusted [] [] [] [].0 [] 0.04 [] 0. [] 0.4 [] 3.35 [] 0.15 [] 0.5 [] 0. [] 1.5 [] 3.0 [] MvD 7
Reynolds, an engineering professor in early 1880 demonstrated two different types of flow through an experiment:
7 STEADY FLOW IN PIPES 7.1 Reynolds Number Reynolds, an engineering professor in early 1880 demonstrated two different types of flow through an experiment: Laminar flow Turbulent flow Reynolds apparatus
More informationWater Circuit Lab. The pressure drop along a straight pipe segment can be calculated using the following set of equations:
Water Circuit Lab When a fluid flows in a conduit, there is friction between the flowing fluid and the pipe walls. The result of this friction is a net loss of energy in the flowing fluid. The fluid pressure
More informationChapter 10 Flow in Conduits
Chapter 10 Flow in Conduits 10.1 Classifying Flow Laminar Flow and Turbulent Flow Laminar flow Unpredictable Turbulent flow Near entrance: undeveloped developing flow In developing flow, the wall shear
More informationHydraulics and hydrology
Hydraulics and hydrology - project exercises - Class 4 and 5 Pipe flow Discharge (Q) (called also as the volume flow rate) is the volume of fluid that passes through an area per unit time. The discharge
More informationChapter 6. Losses due to Fluid Friction
Chapter 6 Losses due to Fluid Friction 1 Objectives ä To measure the pressure drop in the straight section of smooth, rough, and packed pipes as a function of flow rate. ä To correlate this in terms of
More informationHydraulics. B.E. (Civil), Year/Part: II/II. Tutorial solutions: Pipe flow. Tutorial 1
Hydraulics B.E. (Civil), Year/Part: II/II Tutorial solutions: Pipe flow Tutorial 1 -by Dr. K.N. Dulal Laminar flow 1. A pipe 200mm in diameter and 20km long conveys oil of density 900 kg/m 3 and viscosity
More informationDaniel López Gaxiola 1 Student View Jason M. Keith
Suppleental Material for Transport Process and Separation Process Principles Chapter Principles of Moentu Transfer and Overall Balances In fuel cells, the fuel is usually in gas or liquid phase. Thus,
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 informationLECTURE 6- ENERGY LOSSES IN HYDRAULIC SYSTEMS SELF EVALUATION QUESTIONS AND ANSWERS
LECTURE 6- ENERGY LOSSES IN HYDRAULIC SYSTEMS SELF EVALUATION QUESTIONS AND ANSWERS 1. What is the head loss ( in units of bars) across a 30mm wide open gate valve when oil ( SG=0.9) flow through at a
More informationChapter 6. Losses due to Fluid Friction
Chapter 6 Losses due to Fluid Friction 1 Objectives To measure the pressure drop in the straight section of smooth, rough, and packed pipes as a function of flow rate. To correlate this in terms of the
More informationViscous Flow in Ducts
Dr. M. Siavashi Iran University of Science and Technology Spring 2014 Objectives 1. Have a deeper understanding of laminar and turbulent flow in pipes and the analysis of fully developed flow 2. Calculate
More informationFLUID MECHANICS D203 SAE SOLUTIONS TUTORIAL 2 APPLICATIONS OF BERNOULLI SELF ASSESSMENT EXERCISE 1
FLUID MECHANICS D203 SAE SOLUTIONS TUTORIAL 2 APPLICATIONS OF BERNOULLI SELF ASSESSMENT EXERCISE 1 1. A pipe 100 mm bore diameter carries oil of density 900 kg/m3 at a rate of 4 kg/s. The pipe reduces
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 informationPipe Flow. Lecture 17
Pipe Flow Lecture 7 Pipe Flow and the Energy Equation For pipe flow, the Bernoulli equation alone is not sufficient. Friction loss along the pipe, and momentum loss through diameter changes and corners
More informationFriction Factors and Drag Coefficients
Levicky 1 Friction Factors and Drag Coefficients Several equations that we have seen have included terms to represent dissipation of energy due to the viscous nature of fluid flow. For example, in the
More informationP & I Design Limited. 2 Reed Street, Gladstone Industrial Estate, Thornaby, TS17 7AF. Tel: +44 (0) Fax: +44 (0)
ump Sizing & Rating USER MANUAL & I Design Limited Reed Street, Gladstone Industrial Estate, Thornaby, TS7 7AF. Tel: +44 (0) 64 67444 Fax: +44 (0) 64 66447 www.pidesign.co.uk Support: sales@pidesign.co.uk
More information2 Internal Fluid Flow
Internal Fluid Flow.1 Definitions Fluid Dynamics The study of fluids in motion. Static Pressure The pressure at a given point exerted by the static head of the fluid present directly above that point.
More informationWhen water (fluid) flows in a pipe, for example from point A to point B, pressure drop will occur due to the energy losses (major and minor losses).
PRESSURE DROP AND OSSES IN PIPE When water (luid) lows in a pipe, or example rom point A to point B, pressure drop will occur due to the energy losses (major and minor losses). A B Bernoulli equation:
More informationACCOUNTING FOR FRICTION IN THE BERNOULLI EQUATION FOR FLOW THROUGH PIPES
ACCOUNTING FOR FRICTION IN THE BERNOULLI EQUATION FOR FLOW THROUGH PIPES Some background information first: We have seen that a major limitation of the Bernoulli equation is that it does not account for
More informationExternal Flow and Boundary Layer Concepts
1 2 Lecture (8) on Fayoum University External Flow and Boundary Layer Concepts By Dr. Emad M. Saad Mechanical Engineering Dept. Faculty of Engineering Fayoum University Faculty of Engineering Mechanical
More informationUniversität Duisburg-Essen Fakultät für Ingenieurwissenschaften WS 2012 Maschinenbau, IVG, Thermodynamik Dr. M. A. Siddiqi
1 Universität Duisburg-Essen 3. Semester Fakultät für Ingenieurwissenschaften WS 2012 Maschinenbau, IVG, Thermodynamik Dr. M. A. Siddiqi THERMODYNAMICS LAB (ISE) Pressure Measurement 2 2 Pressure Measurement
More informationChapter 8: Flow in Pipes
8-1 Introduction 8-2 Laminar and Turbulent Flows 8-3 The Entrance Region 8-4 Laminar Flow in Pipes 8-5 Turbulent Flow in Pipes 8-6 Fully Developed Pipe Flow 8-7 Minor Losses 8-8 Piping Networks and Pump
More informationPiping Systems and Flow Analysis (Chapter 3)
Piping Systems and Flow Analysis (Chapter 3) 2 Learning Outcomes (Chapter 3) Losses in Piping Systems Major losses Minor losses Pipe Networks Pipes in series Pipes in parallel Manifolds and Distribution
More informationBernoulli and Pipe Flow
Civil Engineering Hydraulics Mechanics of Fluids Head Loss Calculations Bernoulli and The Bernoulli equation that we worked with was a bit simplistic in the way it looked at a fluid system All real systems
More informationOnly if handing in. Name: Student No.: Page 2 of 7
UNIVERSITY OF TORONTO FACULTY OF APPLIED SCIENCE AND ENGINEERING FINAL EXAMINATION, DECEMBER 10, 2014 2:00 PM 2.5 HOURS CHE 211F FLUID MECHANICS EXAMINER: PROFESSOR D.G. ALLEN ANSWER ALL SEVEN (7) QUESTIONS
More informationNon Newtonian Fluid Dynamics
PDHonline Course M417 (3 PDH) Non Newtonian Fluid Dynamics Instructor: Paul G. Conley, PE 2012 PDH Online PDH Center 5272 Meadow Estates Drive Fairfax, VA 22030-6658 Phone & Fax: 703-988-0088 www.pdhonline.org
More informationChapter 8: Flow in Pipes
Objectives 1. Have a deeper understanding of laminar and turbulent flow in pipes and the analysis of fully developed flow 2. Calculate the major and minor losses associated with pipe flow in piping networks
More informationCalculation of Pipe Friction Loss
Doc.No. 6122-F3T071 rev.2 Calculation of Pipe Friction Loss Engineering Management Group Development Planning Department Standard Pump Business Division EBARA corporation October 16th, 2013 1 / 33 2 /
More informationFE Fluids Review March 23, 2012 Steve Burian (Civil & Environmental Engineering)
Topic: Fluid Properties 1. If 6 m 3 of oil weighs 47 kn, calculate its specific weight, density, and specific gravity. 2. 10.0 L of an incompressible liquid exert a force of 20 N at the earth s surface.
More informationPIPE FLOW. General Characteristic of Pipe Flow. Some of the basic components of a typical pipe system are shown in Figure 1.
PIPE FLOW General Characteristic of Pipe Flow Figure 1 Some of the basic components of a typical pipe system are shown in Figure 1. They include the pipes, the various fitting used to connect the individual
More informationEasy Evaluation Method of Self-Compactability of Self-Compacting Concrete
Easy Evaluation Method of Self-Copactability of Self-Copacting Concrete Masanori Maruoka 1 Hiroi Fujiwara 2 Erika Ogura 3 Nobu Watanabe 4 T 11 ABSTRACT The use of self-copacting concrete (SCC) in construction
More informationTable of Contents. Foreword... xiii. Preface... xv
Table of Contents Foreword.... xiii Preface... xv Chapter 1. Fundamental Equations, Dimensionless Numbers... 1 1.1. Fundamental equations... 1 1.1.1. Local equations... 1 1.1.2. Integral conservation equations...
More informationFE Exam Fluids Review October 23, Important Concepts
FE Exam Fluids Review October 3, 013 mportant Concepts Density, specific volume, specific weight, specific gravity (Water 1000 kg/m^3, Air 1. kg/m^3) Meaning & Symbols? Stress, Pressure, Viscosity; Meaning
More informationFigure 3: Problem 7. (a) 0.9 m (b) 1.8 m (c) 2.7 m (d) 3.6 m
1. For the manometer shown in figure 1, if the absolute pressure at point A is 1.013 10 5 Pa, the absolute pressure at point B is (ρ water =10 3 kg/m 3, ρ Hg =13.56 10 3 kg/m 3, ρ oil = 800kg/m 3 ): (a)
More information2 Navier-Stokes Equations
1 Integral analysis 1. Water enters a pipe bend horizontally with a uniform velocity, u 1 = 5 m/s. The pipe is bended at 90 so that the water leaves it vertically downwards. The input diameter d 1 = 0.1
More informationPart A: 1 pts each, 10 pts total, no partial credit.
Part A: 1 pts each, 10 pts total, no partial credit. 1) (Correct: 1 pt/ Wrong: -3 pts). The sum of static, dynamic, and hydrostatic pressures is constant when flow is steady, irrotational, incompressible,
More informationMajor and Minor Losses
Abstract Major and Minor Losses Caitlyn Collazo, Team 2 (1:00 pm) A Technovate fluid circuit system was used to determine the pressure drop across a pipe section and across an orifice. These pressure drops
More information2, where dp is the constant, R is the radius of
Dynamics of Viscous Flows (Lectures 8 to ) Q. Choose the correct answer (i) The average velocity of a one-dimensional incompressible fully developed viscous flow between two fixed parallel plates is m/s.
More informationTHE EFFECT OF SOLID PARTICLE SIZE UPON TIME AND SEDIMENTATION RATE
Bulletin of the Transilvania University of Braşov Series II: Forestry Wood Industry Agricultural Food Engineering Vol. 5 (54) No. 1-1 THE EFFECT OF SOLID PARTICLE SIZE UPON TIME AND SEDIMENTATION RATE
More informationExercise sheet 5 (Pipe flow)
Exercise sheet 5 (Pipe flow) last edited June 4, 2018 These lecture notes are based on textbooks by White [13], Çengel & al.[16], and Munson & al.[18]. Except otherwise indicated, we assume that fluids
More informationProf. Scalo Prof. Vlachos Prof. Ardekani Prof. Dabiri 08:30 09:20 A.M 10:30 11:20 A.M. 1:30 2:20 P.M. 3:30 4:20 P.M.
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. Scalo Prof. Vlachos
More informationChapter 10: Flow Flow in in Conduits Conduits Dr Ali Jawarneh
Chater 10: Flow in Conduits By Dr Ali Jawarneh Hashemite University 1 Outline In this chater we will: Analyse the shear stress distribution across a ie section. Discuss and analyse the case of laminar
More informationF L U I D S Y S T E M D Y N A M I C S
F L U I D S Y S T E M D Y N A M I C S T he proper design, construction, operation, and maintenance of fluid systems requires understanding of the principles which govern them. These principles include
More informationPIPING SYSTEMS. Pipe and Tubing Standards Sizes for pipes and tubes are standardized. Pipes are specified by a nominal diameter and a schedule number.
PIPING SYSTEMS In this chapter we will review some of the basic concepts associated with piping systems. Topics that will be considered in this chapter are - Pipe and tubing standards - Effective and hydraulic
More informationSignature: (Note that unsigned exams will be given a score of zero.)
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. Dabiri Prof. Wassgren Prof.
More informationTALLINN UNIVERSITY OF TECHNOLOGY, DIVISION OF PHYSICS 13. STOKES METHOD
13. STOKES METHOD 1. Objective To determine the coefficient of viscosity of a known fluid using Stokes method.. Equipment needed A glass vessel with glycerine, micrometer calliper, stopwatch, ruler. 3.
More informationME 305 Fluid Mechanics I. Part 8 Viscous Flow in Pipes and Ducts. Flow in Pipes and Ducts. Flow in Pipes and Ducts (cont d)
ME 305 Fluid Mechanics I Flow in Pipes and Ducts Flow in closed conduits (circular pipes and non-circular ducts) are very common. Part 8 Viscous Flow in Pipes and Ducts These presentations are prepared
More informationFLUID MECHANICS PROF. DR. METİN GÜNER COMPILER
FLUID MECHANICS PROF. DR. METİN GÜNER COMPILER ANKARA UNIVERSITY FACULTY OF AGRICULTURE DEPARTMENT OF AGRICULTURAL MACHINERY AND TECHNOLOGIES ENGINEERING 1 5. FLOW IN PIPES 5.1.3. Pressure and Shear Stress
More informationLaminar and turbulent flows
Ventilation 0 Duct Design Vladimír Zmrhal (room no. 84) http://users.fs.cvut.cz/~zmrhavla/index.htm Dpt. Of Environmental Engineering Laminar and turbulent flos Reynolds number d Re = ν laminar flo Re
More informationIntroduction to Fluid Flow
Introduction to Fluid Flow Learning Outcomes After this lecture you should be able to Explain viscosity and how it changes with temperature Write the continuity equation Define laminar and turbulent flow
More informationτ du In his lecture we shall look at how the forces due to momentum changes on the fluid and viscous forces compare and what changes take place.
4. Real fluids The flow of real fluids exhibits viscous effect, that is they tend to stick to solid surfaces and have stresses within their body. You might remember from earlier in the course Newtons law
More informationEffect of Polymer Solutions on Efflux Time for Two Exit Pipe System
Effect of Polyer Solutions on Efflux Tie for Two Exit Pipe Syste Abstract: A. UMA DEVI a, D.V. PADMA a & CH. V. SUBBARAO a a Departent of Cheical Engineering, MVGR College of Engineering, Vizianagara-535005,
More informationChapter 6. Hydraulic cylinders/rams (linear motors), and Lines/fittings. - Transforms the flow of a pressurized fluid into a push or pull of a rod.
Chapter 6. Hydraulic cylinders/rams (linear motors), and Lines/fittings - Transforms the flow of a pressurized fluid into a push or pull of a rod. 6. Single cting Rams Gravity, spring, etc. can force piston
More informationSourabh V. Apte. 308 Rogers Hall
Sourabh V. Apte 308 Rogers Hall sva@engr.orst.edu 1 Topics Quick overview of Fluid properties, units Hydrostatic forces Conservation laws (mass, momentum, energy) Flow through pipes (friction loss, Moody
More informationME 309 Fluid Mechanics Fall 2010 Exam 2 1A. 1B.
Fall 010 Exam 1A. 1B. Fall 010 Exam 1C. Water is flowing through a 180º bend. The inner and outer radii of the bend are 0.75 and 1.5 m, respectively. The velocity profile is approximated as C/r where C
More informationUNIT II Real fluids. FMM / KRG / MECH / NPRCET Page 78. Laminar and turbulent flow
UNIT II Real fluids The flow of real fluids exhibits viscous effect that is they tend to "stick" to solid surfaces and have stresses within their body. You might remember from earlier in the course Newtons
More informationSignature: (Note that unsigned exams will be given a score of zero.)
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. Dabiri Prof. Wassgren Prof.
More informationMEASUREMENT OF VISCOSITY OF LIQUID
MEASUREMENT OF VISCOSITY OF LIQUID Objectives: To measure the viscosity of sample liquids. Apparatus: (i) Glass tube (ii)steel balls, (iii) Retort stand and clamps, (iv) Weighing balance, (v) Screw gauge,
More informationLecture 13 Flow Measurement in Pipes. I. Introduction
Lecture 13 Flow Measurement in Pipes I. Introduction There are a wide variety of methods for measuring discharge and velocity in pipes, or closed conduits Many of these methods can provide very accurate
More informationChapter 3 Non-Newtonian fluid
Chapter 3 Non-Newtonian fluid 3-1. Introduction: The study of the deformation of flowing fluids is called rheology; the rheological behavior of various fluids is sketchen Figure 3-1. Newtonian fluids,
More informationMechanical Engineering Programme of Study
Mechanical Engineering Programme of Study Fluid Mechanics Instructor: Marios M. Fyrillas Email: eng.fm@fit.ac.cy SOLVED EXAMPLES ON VISCOUS FLOW 1. Consider steady, laminar flow between two fixed parallel
More informationLesson 6 Review of fundamentals: Fluid flow
Lesson 6 Review of fundamentals: Fluid flow The specific objective of this lesson is to conduct a brief review of the fundamentals of fluid flow and present: A general equation for conservation of mass
More informationDesign PEL PEW. Reference Guide 3BGB D0012
IT Design PEL PEW Reference Guide 3BGB0000 - D001 About this document This document summarises the mathematical theory used by the PEW program. It has been produced to the recommendations of British Standard
More informationCVE 372 HYDROMECHANICS EXERCISE PROBLEMS
VE 37 HYDROMEHNIS EXERISE PROLEMS 1. pump that has the characteristic curve shown in the accompanying graph is to be installed in the system shown. What will be the discharge of water in the system? Take
More informationHydraulic Design Of Polyethylene Pipes
Hydraulic Design Of Polyethylene Pipes Waters & Farr polyethylene pipes offer a hydraulically smooth bore that provides excellent flow characteristics. Other advantages of Waters & Farr polyethylene pipes,
More informationApplied Fluid Mechanics
Applied Fluid Mechanics 1. The Nature of Fluid and the Study of Fluid Mechanics 2. Viscosity of Fluid 3. Pressure Measurement 4. Forces Due to Static Fluid 5. Buoyancy and Stability 6. Flow of Fluid and
More informationOutlines. simple relations of fluid dynamics Boundary layer analysis. Important for basic understanding of convection heat transfer
Forced Convection Outlines To examine the methods of calculating convection heat transfer (particularly, the ways of predicting the value of convection heat transfer coefficient, h) Convection heat transfer
More information9. Pumps (compressors & turbines) Partly based on Chapter 10 of the De Nevers textbook.
Lecture Notes CHE 31 Fluid Mechanics (Fall 010) 9. Pumps (compressors & turbines) Partly based on Chapter 10 of the De Nevers textbook. Basics (pressure head, efficiency, working point, stability) Pumps
More informationME 305 Fluid Mechanics I. Chapter 8 Viscous Flow in Pipes and Ducts
ME 305 Fluid Mechanics I Chapter 8 Viscous Flow in Pipes and Ducts These presentations are prepared by Dr. Cüneyt Sert Department of Mechanical Engineering Middle East Technical University Ankara, Turkey
More informationPhysics 3 Summer 1990 Lab 7 - Hydrodynamics
Physics 3 Summer 1990 Lab 7 - Hydrodynamics Theory Consider an ideal liquid, one which is incompressible and which has no internal friction, flowing through pipe of varying cross section as shown in figure
More informationFluid Flow. Fundamentals of Rheology. Rheology is the science of deformation and flow. Food rheology is the material science of food
Fluid Flow Outline Fundamentals and applications of rheology Shear stress and shear rate Viscosity and types of viscometers Rheological classification of fluids Apparent viscosity Effect of temperature
More informationChapter 1: Basic Concepts
What is a fluid? A fluid is a substance in the gaseous or liquid form Distinction between solid and fluid? Solid: can resist an applied shear by deforming. Stress is proportional to strain Fluid: deforms
More informationEXPERIMENT II - FRICTION LOSS ALONG PIPE AND LOSSES AT PIPE FITTINGS
MM 30 FLUID MECHANICS II Prof. Dr. Nuri YÜCEL Yrd. Doç. Dr. Nureddin DİNLER Arş. Gör. Dr. Salih KARAASLAN Arş. Gör. Fatih AKTAŞ EXPERIMENT II - FRICTION LOSS ALONG PIPE AND LOSSES AT PIPE FITTINGS A. Objective:
More informationPrinciples of Food and Bioprocess Engineering (FS 231) Problems on Heat Transfer
Principles of Food and Bioprocess Engineering (FS 1) Problems on Heat Transfer 1. What is the thermal conductivity of a material 8 cm thick if the temperature at one end of the product is 0 C and the temperature
More informationCustom Search Sponsored Links
Dynamic, Absolute and Kinematic Viscosity An introduction to dynamic, absolute and kinematic viscosity and how to convert between CentiStokes (cst), CentiPoises (cp), Saybolt Universal Seconds (SSU), degree
More informationParticle removal in linear shear flow: model prediction and experimental validation
Particle removal in linear shear flow: model prediction and experimental validation M.L. Zoeteweij, J.C.J. van der Donck and R. Versluis TNO Science and Industry, P.O. Box 155, 600 AD Delft, The Netherlands
More informationCHAPTER THREE FLUID MECHANICS
CHAPTER THREE FLUID MECHANICS 3.1. Measurement of Pressure Drop for Flow through Different Geometries 3.. Determination of Operating Characteristics of a Centrifugal Pump 3.3. Energy Losses in Pipes under
More informationFluid Flow Analysis Penn State Chemical Engineering
Fluid Flow Analysis Penn State Chemical Engineering Revised Spring 2015 Table of Contents LEARNING OBJECTIVES... 1 EXPERIMENTAL OBJECTIVES AND OVERVIEW... 1 PRE-LAB STUDY... 2 EXPERIMENTS IN THE LAB...
More informationFLOW IN CONDUITS. Shear stress distribution across a pipe section. Chapter 10
Chapter 10 Shear stress distribution across a pipe section FLOW IN CONDUITS For steady, uniform flow, the momentum balance in s for the fluid cylinder yields Fluid Mechanics, Spring Term 2010 Velocity
More informationSENTHIL SELIYAN ELANGO ID: UB3016SC17508 AIU HYDRAULICS (FLUID DYNAMICS)
SENTHIL SELIYAN ELANGO ID: UB3016SC17508 AIU HYDRAULICS (FLUID DYNAMICS) ATLANTIC INTERNATIONAL UNIVERSITY INTRODUCTION Real fluids The flow of real fluids exhibits viscous effect, which are they tend
More informationPipe Flow Design 1. Results Data
Pipe Flow Design 1 Results Data Color of Pipe: Velocity in m/sec 1.9 2.2 2.4 2.7 2.9 3.2 Pipe Flow Expert Results Key f = flow in Modelling a 'Tee' fitting: The flow rate through the 'Tee' w ill be different
More informationApproximate physical properties of selected fluids All properties are given at pressure kn/m 2 and temperature 15 C.
Appendix FLUID MECHANICS Approximate physical properties of selected fluids All properties are given at pressure 101. kn/m and temperature 15 C. Liquids Density (kg/m ) Dynamic viscosity (N s/m ) Surface
More informationLECTURE 1 THE CONTENTS OF THIS LECTURE ARE AS FOLLOWS:
LECTURE 1 THE CONTENTS OF THIS LECTURE ARE AS FOLLOWS: 1.0 INTRODUCTION TO FLUID AND BASIC EQUATIONS 2.0 REYNOLDS NUMBER AND CRITICAL VELOCITY 3.0 APPROACH TOWARDS REYNOLDS NUMBER REFERENCES Page 1 of
More informationChemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017
Chemical and Biomolecular Engineering 150A Transport Processes Spring Semester 2017 Objective: Text: To introduce the basic concepts of fluid mechanics and heat transfer necessary for solution of engineering
More informationFLUID MECHANICS PROF. DR. METİN GÜNER COMPILER
FLUID MECHANICS PROF. DR. METİN GÜNER COMPILER ANKARA UNIVERSITY FACULTY OF AGRICULTURE DEPARTMENT OF AGRICULTURAL MACHINERY AND TECHNOLOGIES ENGINEERING 1 5. FLOW IN PIPES Liquid or gas flow through pipes
More informationConvective Mass Transfer
Convective Mass Transfer Definition of convective mass transfer: The transport of material between a boundary surface and a moving fluid or between two immiscible moving fluids separated by a mobile interface
More informationAn Expression for Obtaining Total Heads for Lift Pump Selection
American Journal of Engineering Research (AJER) e-issn : 2320-0847 p-issn : 2320-0936 Volume-03, Issue-06, pp-169-176 www.ajer.org Research Paper Open Access An Expression for Obtaining Total Heads for
More informationREE 307 Fluid Mechanics II. Lecture 1. Sep 27, Dr./ Ahmed Mohamed Nagib Elmekawy. Zewail City for Science and Technology
REE 307 Fluid Mechanics II Lecture 1 Sep 27, 2017 Dr./ Ahmed Mohamed Nagib Elmekawy Zewail City for Science and Technology Course Materials drahmednagib.com 2 COURSE OUTLINE Fundamental of Flow in pipes
More informationLEAKLESS COOLING SYSTEM V.2 PRESSURE DROP CALCULATIONS AND ASSUMPTIONS
CH-1211 Geneva 23 Switzerland EDMS No. ST/CV - Cooling of Electronics & Detectors GUIDE LEAKLESS COOLING SYSTEM V.2 PRESSURE DROP CALCULATIONS AND ASSUMPTIONS Objectives Guide to Leakless Cooling System
More informationCE 6403 APPLIED HYDRAULIC ENGINEERING UNIT - V PUMPS
CE 6403 APPLIED HYDRAULIC ENGINEERING UNIT - V PUMPS Centrifugal pups - Miniu speed to start the pup - NPSH - Cavitations in pups Operating characteristics - Multistage pups - Reciprocating pups - Negative
More informationLecture 4. Lab this week: Cartridge valves Flow divider Properties of Hydraulic Fluids. Lab 8 Sequencing circuit Lab 9 Flow divider
91 Lecture 4 Lab this week: Lab 8 Sequencing circuit Lab 9 Flow divider Cartridge valves Flow divider Properties of Hydraulic Fluids Viscosity friction and leakage Bulk modulus Inertance Cartridge Valves
More informationThe Mechatronics Design for Measuring Fluid Friction Losses in Pipe Flows Rıza Gurbuz
Solid State Phenomena Vol. 113 (2006) pp 603-608 Online available since 2006/Jun/15 at www.scientific.net (2006) Trans Tech Publications, Switzerland doi:10.4028/www.scientific.net/ssp.113.603 The Mechatronics
More informationWhat s important: viscosity Poiseuille's law Stokes' law Demo: dissipation in flow through a tube
PHYS 101 Lecture 29x - Viscosity 29x - 1 Lecture 29x Viscosity (extended version) What s important: viscosity Poiseuille's law Stokes' law Demo: dissipation in flow through a tube Viscosity We introduced
More informationTankExampleNov2016. Table of contents. Layout
Table of contents Task... 2 Calculation of heat loss of storage tanks... 3 Properties ambient air Properties of air... 7 Heat transfer outside, roof Heat transfer in flow past a plane wall... 8 Properties
More informationFACULTY OF CHEMICAL & ENERGY ENGINEERING FLUID MECHANICS LABORATORY TITLE OF EXPERIMENT: MINOR LOSSES IN PIPE (E4)
FACULTY OF CHEMICAL & ENERGY ENGINEERING FLUID MECHANICS LABORATORY TITLE OF EXPERIMENT: MINOR LOSSES IN PIPE (E4) 1 1.0 Objectives The objective of this experiment is to calculate loss coefficient (K
More informationME332 FLUID MECHANICS LABORATORY (PART II)
ME332 FLUID MECHANICS LABORATORY (PART II) Mihir Sen Department of Aerospace and Mechanical Engineering University of Notre Dame Notre Dame, IN 46556 Version: April 2, 2002 Contents Unit 5: Momentum transfer
More informationINSTITUTE OF AERONAUTICAL ENGINEERING Dundigal, Hyderabad AERONAUTICAL ENGINEERING QUESTION BANK : AERONAUTICAL ENGINEERING.
Course Name Course Code Class Branch INSTITUTE OF AERONAUTICAL ENGINEERING Dundigal, Hyderabad - 00 0 AERONAUTICAL ENGINEERING : Mechanics of Fluids : A00 : II-I- B. Tech Year : 0 0 Course Coordinator
More informationTutorial for the heated pipe with constant fluid properties in STAR-CCM+
Tutorial for the heated pipe with constant fluid properties in STAR-CCM+ For performing this tutorial, it is necessary to have already studied the tutorial on the upward bend. In fact, after getting abilities
More informationR09. d water surface. Prove that the depth of pressure is equal to p +.
Code No:A109210105 R09 SET-1 B.Tech II Year - I Semester Examinations, December 2011 FLUID MECHANICS (CIVIL ENGINEERING) Time: 3 hours Max. Marks: 75 Answer any five questions All questions carry equal
More informationMM303 FLUID MECHANICS I PROBLEM SET 1 (CHAPTER 2) FALL v=by 2 =-6 (1/2) 2 = -3/2 m/s
MM303 FLUID MECHANICS I PROBLEM SET 1 (CHAPTER ) FALL 018 1) For the velocity fields given below, determine: i) Whether the flow field is one-, two-, or three-dimensional, and why. ii) Whether the flow
More information