Flow Velocity Measurement Principles of Hot Film Anemometry

Similar documents
Chapter 1 Fundamentals

Understanding Hot-Wire Anemometry

The extreme case of the anisothermal calorimeter when there is no heat exchange is the adiabatic calorimeter.

1 atm = 1.01x10 Pa = 760 Torr = 14.7 lb / in

Chapter 20: Exercises: 3, 7, 11, 22, 28, 34 EOC: 40, 43, 46, 58

EE 508 Lecture 13. Statistical Characterization of Filter Characteristics

12.808: Some Physical Properties of Sea Water or, More than you ever wanted to know about the basic state variables of the ocean

THE FIRST LAW OF THERMODYNAMICS

1. Mark the correct statement(s)

P-MOS Device and CMOS Inverters

LMM-H04 Mass Air Flow Sensor

Homogeneous and Inhomogeneous Model for Flow and Heat Transfer in Porous Materials as High Temperature Solar Air Receivers

Phase transition. Asaf Pe er Background

Chapter 10: Flow Flow in in Conduits Conduits Dr Ali Jawarneh

16. CHARACTERISTICS OF SHOCK-WAVE UNDER LORENTZ FORCE AND ENERGY EXCHANGE

AE301 Aerodynamics I UNIT A: Fundamental Concepts

ANALYTICAL MODEL FOR THE BYPASS VALVE IN A LOOP HEAT PIPE

dn i where we have used the Gibbs equation for the Gibbs energy and the definition of chemical potential

Review Outline. 1. Chapter 1: Signals and Amplifiers. 2. Chapter 3: Semiconductors. 3. Chapter 4: Diodes. EE 3110 Microelectronics I

Actual exergy intake to perform the same task

The Numerical Simulation of Gas Turbine Inlet-Volute Flow Field

FUGACITY. It is simply a measure of molar Gibbs energy of a real gas.

Participation Factors. However, it does not give the influence of each state on the mode.

Lecture 22. Mechanical Energy Balance

APPENDIX 1 DESCRIPTION OF HOT WIRE ANEMOMETER

Chapter 3: Fundamentals of Mechanics and Heat. 1/11/00 Electromechanical Dynamics 1

Notes on pressure coordinates Robert Lindsay Korty October 1, 2002

Oil Temperature Control System PID Controller Algorithm Analysis Research on Sliding Gear Reducer

MODULE 2: DIFFUSION LECTURE NO. 2

Polytech Montpellier MEA4 M2 EEA Systèmes Microélectroniques. Analog IC Design

200kW HIGH FREQUENCY PRESS FOR DIELECTRIC HEATING. J. Tomljenovic

CHME 302 CHEMICAL ENGINEERING LABOATORY-I EXPERIMENT 302-V FREE AND FORCED CONVECTION

High speed wind tunnels 2.0 Definition of high speed. 2.1 Types of high speed wind tunnels

Session 12 : Monopropellant Thrusters

P1.33 ECONOMICAL THERMAL MASS FLOW SENSOR BASED ON CONSTANT TEMPERATURE ANEMOMETRY

Unit code: H/ QCF level: 5 Credit value: 15 OUTCOME 1 - THERMODYNAMIC SYSTEMS TUTORIAL 2

Week 8 lectures. ρ t +u ρ+ρ u = 0. where µ and λ are viscosity and second viscosity coefficients, respectively and S is the strain tensor:

2d-Laser Cantilever Anemometer

Feedback-error control

EE 508 Lecture 13. Statistical Characterization of Filter Characteristics

FET ( Field Effect Transistor)

1. Read the section on stability in Wallace and Hobbs. W&H 3.53

Effects of screens set characteristics on the flow field in a wind tunnel.

(Refer slide Time 1:09)

An-Najah National University Civil Engineering Departemnt. Fluid Mechanics. Chapter [2] Fluid Statics

Measurement of cyclone separator

AE301 Aerodynamics I UNIT A: Fundamental Concepts

Simulation of the PIR detector active function

MODEL-BASED MULTIPLE FAULT DETECTION AND ISOLATION FOR NONLINEAR SYSTEMS

GEF2200 vår 2017 Løsningsforslag sett 1

The thermal wind 1. v g

Lecture Thermodynamics 9. Entropy form of the 1 st law. Let us start with the differential form of the 1 st law: du = d Q + d W

The Role of Water Vapor. atmosphere (we will ignore the solid phase here) Refer to the phase diagram in the web notes.

MANDATORY APPENDIX 41 ELECTRIC IMMERSION HEATER ELEMENT SUPPORT PLATES

Speed of sound measurements in liquid Methane at cryogenic temperature and for pressure up to 10 MPa

Comparison of Maximum Allowable Pump Speed in a Horizontal and Vertical Pipe of Equal Geometry at Constant Power

Wolfgang POESSNECKER and Ulrich GROSS*

Lecture #05. Methods for local Flow Velocity Measurements. AerE 545 class notes

First law of thermodynamics (Jan 12, 2016) page 1/7. Here are some comments on the material in Thompkins Chapter 1

Setting up the Mathematical Model Review of Heat & Material Balances

Background Information for Use of Pitot Tube, Manometer, Hot Wires, and Hot Films

Chapter-6: Entropy. 1 Clausius Inequality. 2 Entropy - A Property

Estimation of dynamic behavior and energy efficiency of thrust hybrid bearings with active control

ATS WHITE PAPER. Air Flow Measurement in Electronic Systems

MODELLING, SIMULATION AND ROBUST ANALYSIS OF THE TEMPERATURE PROCESS CONTROL

Measurement and Industrial Instrumentation

Outline. EECS150 - Digital Design Lecture 26 Error Correction Codes, Linear Feedback Shift Registers (LFSRs) Simple Error Detection Coding

ANALYSIS OF ENTROPY GENERATION IN A CIRCULAR TUBE WITH SHORT LENGTH TWISTED TAPE INSERTS

SECTION 1.2. DYNAMIC MODELS

Theory of turbomachinery. Chapter 1

DSP IC, Solutions. The pseudo-power entering into the adaptor is: 2 b 2 2 ) (a 2. Simple, but long and tedious simplification, yields p = 0.

ONE. The Earth-atmosphere system CHAPTER

Introduction to Silvaco ATHENA Tool and Basic Concepts in Process Modeling Part - 1. Instructor: Dragica Vasileska

Controllability and Resiliency Analysis in Heat Exchanger Networks

Principle And Practice Of Hotwire Anemometry In Turbomachinery Applications

FE FORMULATIONS FOR PLASTICITY

Lecture 2. OUTLINE Basic Semiconductor Physics (cont d) PN Junction Diodes. Reading: Chapter Carrier drift and diffusion

Fuzzy Methods. Additions to Chapter 5: Fuzzy Arithmetic. Michael Hanss.

ECE 534 Information Theory - Midterm 2

4/8/2012. Example. Definition of the current: dq I = dt

02. Equilibrium Thermodynamics II: Engines

Lecture 13. Heat Engines. Thermodynamic processes and entropy Thermodynamic cycles Extracting work from heat

The Second Law: The Machinery

PHYSICAL REVIEW LETTERS

Chapter 9 Practical cycles

A comparison of two barometers: Nicholas Fortin versus Robert Bosch

Preliminary Uncertainty Estimation of the Pressure Distortion Coefficient of a Pressure. Balance by FEM Calculations

Laser Doppler Anemometry. Introduction to principles and applications

By Mehak Chopra Indian Institute of Technology Delhi. Guide: Dr B. Uensal

Paper C Exact Volume Balance Versus Exact Mass Balance in Compositional Reservoir Simulation

The Thermo Economical Cost Minimization of Heat Exchangers

1 Properties of Spherical Harmonics

Introduction to MVC. least common denominator of all non-identical-zero minors of all order of G(s). Example: The minor of order 2: 1 2 ( s 1)

Fluctuating Heat Transfer to an Impinging Air Jet in the Transitional Wall Jet Region

4. A Brief Review of Thermodynamics, Part 2

Chapter 6. Thermodynamics and the Equations of Motion

Multiple Resonance Networks

Solutions to Problem Set 5

VLSI Based Fluid Flow Measurement Using Constant Temperature Hot Wire Anemometer

Transcription:

Flow Velocity Measurement Princiles of Hot Film Anemometry The hot film anemometer (HFA) is made of a thin, structured, metallic resistive film ( heater ) which is deosited onto a substrate. In the oerating state of the HFA the electrical ower P heats the heater u to a temerature t h. A (air-) flow with velocity v and ambient temerature t a cools the heater down until an equilibrium between the electrical Joule heat and the thermal heat loss Q is reached. The higher the velocity v and the difference t h-a =t h -t a ( overheating temerature t h-a ) between the heater temerature t h and the fluid temerature t a, the higher is the heat loss from the heater. The overheating temerature t h-a deends further on the ambient temerature t a, which can change. Therefore t h-a is measured with an additional temerature sensor which is often art of a bridge circuit in order to comensate changes in the ambient temerature automatically. Heat Loss Q Flow v t a P=U I Heater t h-a =t h -t a Substrate U

Flow Velocity Measurement Constant-Temerature-Anemometer The Constant-Temerature-Anemometer (CTA) determines the flow velocity v by measuring the ower P for keeing the overheating temerature t h-a constant. This method achieves higher sensitivities than measuring directly the change of the overheating temerature with flow velocity. The characteristic of the heater is described by the self heating coefficient SHC (t h-a =constant) SHC( v) t h a = P th ta = P( v) which deends on the flow velocity. So after a roer calibration of your system you can determine the flow velocity from the value of the self heating coefficient. 10 8 1/SHC 1/SHC [mw/ C] [kw/ C] 6 4 2 0 0 2 4 6 8 10 12 14 16 18 20 Flow Velocity v [m/s] Tyical 1/SHC(v)-characteristic for t a =25 C, t h-a =40 C Keeing the overheating temerature t h-a constant requires a system control which is usually done using the well known Wheatstone bridge circuit: when flow velocity increases the heater resistance and the overheating temerature t h-a decreases. So the bridge gets out of balance and the amlifier converts the resulting voltage inut signal into an outut signal for increasing the current in a feedback loo so that the overheating temerature t h-a is reached again.

FAQ-What is the influence of atmosheric ressure on the air velocity measurement? Measurement of the air velocity with a hot film-anemometer (which is the rincile of the E+E transmitters) is deendant on the actual air ressure. E+E transmitters are calibrated at 0 =1013.25 mbar. Measuring air velocity at a height h you have to correct the measuring value according to the barometric formula ( 0 =1013 mbar, H=8005 m) : h = 0 e h H Practically you have simly to multily the measured velocity value v T with a correction factor (from the table below) which deends on your actual height h. Examle: If you measure v T =10m/s at a height h=800m, then the real flow velocity is v=10 1,105 m/s=11,05m/s. h [m] [Torr=mm Hg] [hpa=mbar] [atm] [at=k/cm²] correction factor 0 760,0 1013,25 1 1,03323 1,000 50 755,3 1006,94 0,994 1,027 1,006 100 750,6 1000,67 0,988 1,020 1,013 150 745,9 994,44 0,981 1,014 1,019 200 741,2 988,25 0,975 1,008 1,025 300 732,0 975,98 0,963 0,995 1,038 315 730,7 974,15 0,961 0,993 1,040 500 714,0 951,90 0,939 0,971 1,064 800 687,7 916,88 0,905 0,935 1,105 1000 670,8 894,26 0,883 0,912 1,133 1500 630,1 840,11 0,829 0,857 1,206 2000 592,0 789,24 0,779 0,805 1,284 2500 556,1 741,45 0,732 0,756 1,367 3000 522,5 696,56 0,687 0,710 1,455 4000 461,1 614,76 0,607 0,627 1,648 5000 407,0 542,57 0,535 0,553 1,868 6000 359,2 478,85 0,473 0,488 2,116 7000 317,0 422,62 0,417 0,431 2,398 8000 279,8 372,99 0,368 0,380 2,717 9000 246,9 329,19 0,325 0,336 3,078 10000 217,9 290,53 0,287 0,296 3,488

FAQ-How do you convert air velocity into mass flow? You start from the general gas equation V T = konstant the definition of the massflow Q [kg/s] Q = ρ v F the definition of the secific massflow q [kg/(s m²)] q = ρ v [mbar] ressure V [m 3 ] volumne T=t+273.15 [K] absolute temerature t [ C] temerature ρ [kg/m 3 ] density v [m/s] flow velocity F [m 2 ] flow cross section With the air density ρ, absolute temerature T and atmosheric ressure you get with the general gas equation with T0 ρ = ρ0 [kg/m³] T 0 T 0 =273.15 K ρ 0 =1.2922 kg/m 3 absolute normal temerature the density of air at normal conditions 0 =1013.25 mbar the air ressure at normal conditions

The secific mass flow q comes out from a temerature- and ressure indeendent measurement of the air velocity v (which can be done e.g. with a Laser Doler Anemometer (LDA)) : q = 0.3483 v [kg/(s m²)] (273.15 + t) Alication to EE-Transmitters The EE transmitters are temerature comensated, but not ressure comensated. Thus you get a systematic error on your air velocity measurement due to the barometric ressure. The transmitters are calibrated at a normal ressure of 0 = 1013.25 mbar so the measured air velocity is v T = v [m/s] 0 However the real and actual air velocity v is 0 v = vt [m/s] If you insert this into the exression of the secific mass flow you get 353 q = 273.15 + t v T [kg/(s m²)]

FAQ-How do you install E+E air velocity transmitters? Imortant guidelines for rectangular ducts (cross section a b) : D gl = 2 a b /(a + b) Probe in the middle of the channel Preferred mounting after filters, rectifiers, coolers (no twist there) Place the robe in front of diffusers or confusers Filters and coolers calm down the air flow Generally you should have long straight ducts after bends in ies, turn offs, behind flas, fans or changes in cross-sections in order to maintain a laminar flow.

FAQ-What about the angular deendence of E+E air velocity transmitters? The right shae of the transmitter measuring robe is significant for the accuracy of the velocity measurement. It is essential for an accurately measured value when the transmitter is turned around its longitudinal axis out of the right osition. E+E transmitters are excellent in this field and show only a small angular deendance. We otimize our transmitters by use of a Laser Doler Anemometer (LDA) in develoment and calibration for achieving best results. EE65 Angular Deendance 0 0 5 10 15 20 25 30 35-5 Deviation from 0 -value [%] -10-15 -20-25 -30 v=1m/s v=2m/s v=4m/s v=6m/s v=8m/s -35-40 Angle [ ]