Boundary Layer and separation Flow accelerates Flow decelerates Constant flow Flow reversal free shear layer highly unstable Separation point.

Slides:



Advertisements
Similar presentations
HEAT TRANSFER Final Review # 1.
Advertisements

Chapter 7 : Convection – External Flow : Cylinder in cross flow
Convection in Flat Plate Turbulent Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Extra Effect For.
Estimation of Convective Heat Transfer Coefficient
External Convection: Laminar Flat Plate
Chapter 4.2: Flow Across a Tube Bundle Heat Exchanger (Tube Bank)
Chapter 2: Overall Heat Transfer Coefficient
Internal Convection: Fully Developed Flow
Internal Flow: Heat Transfer Correlations
1 Dept. of Energy Technology, Div. of Applied Thermodynamics and Refrigeration Tube diameter influence on heat exchanger performance and design. Single.
Design of Systems with INTERNAL CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Essential Part of Exchanging.
Flow Over Immersed Bodies
Jed Goodell Jesse Williams. Introduction Problem How much heat does a particular heat sink dissipate How many fins are needed to dissipate a specific.
CHE/ME 109 Heat Transfer in Electronics LECTURE 17 – INTERNAL FORCED CONVECTION FUNDAMENTALS.
CHE/ME 109 Heat Transfer in Electronics LECTURE 18 – FLOW IN TUBES.
External Flow: Flow over Bluff Objects (Cylinders, Sphere, Packed Beds) and Impinging Jets.
Why Laminar Flow in Narrow Channels (Heat Transfer Analysis)
CHE/ME 109 Heat Transfer in Electronics
California State University, Chico
Introduction to Convection: Flow and Thermal Considerations
Thermal Development of Internal Flows P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Concept for Precise Design ……
Correlations for INTERNAL CONVECTION P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi An Essential Part of Exchanging Heat……..
Heat Exchangers with Cross Flow past Cylinders P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Another Common Industrial Application!!!
Recent Advances in Condensation on Tube Banks P M V Subbarao Professor Mechanical Engineering Department I I T Delhi Reduce the Degree of Over Design!!!
Pipe Flow Considerations Flow conditions:  Laminar or turbulent: transition Reynolds number Re =  VD/  2,300. That is: Re 4,000 turbulent; 2,300
Cross Flow Heat Exchangers P M V Subbarao Professor Mechanical Engineering Department I I T Delhi A Major Element for the Success of Combustion based.
Chapter 7 Sections 7.4 through 7.8
Fluid Dynamics: Boundary Layers
CHE/ME 109 Heat Transfer in Electronics
Convection Prepared by: Nimesh Gajjar. CONVECTIVE HEAT TRANSFER Convection heat transfer involves fluid motion heat conduction The fluid motion enhances.
Introduction to Convection: Flow and Thermal Considerations
Chapter 4.3: Compact Heat Exchangers
Empirical and Practical Relations for Forced-Convection Heat Transfer
Fouling Factor: After a period of operation the heat transfer surfaces for a heat exchanger become coated with various deposits present in flow systems,
ERT 209 HEAT & MASS TRANSFER Sem 2/ Prepared by; Miss Mismisuraya Meor Ahmad School of Bioprocess Engineering University Malaysia Perlis 17 February.
Convection Part1 External Flow. Introduction Recall: Convention is the heat transfer mode between a fluid and a solid or a 2 fluids of different phases.
Enhancement of Heat Transfer P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi Invention of Compact Heat Transfer Devices……
Chapter 6 Introduction to Forced Convection:
30 th June 20111Enrico Da Riva, V. Rao Parametric study using Empirical Results June 30 th 2011 Bdg 298 Enrico Da Riva,Vinod Singh Rao CFD GTK.
Chapter 7 External Convection
Convective heat exchange within a compact heat exchanger EGEE 520 Instructor: Dr. Derek Elsworth Student: Ana Nedeljkovic-Davidovic 2005.
Heat Transfer/Heat Exchanger How is the heat transfer? Mechanism of Convection Applications. Mean fluid Velocity and Boundary and their effect on the rate.
Convection in Flat Plate Boundary Layers P M V Subbarao Associate Professor Mechanical Engineering Department IIT Delhi A Universal Similarity Law ……
Reynolds Analogy It can be shown that, under specific conditions (no external pressure gradient and Prandtle number equals to one), the momentum and heat.
INTRODUCTION TO CONVECTION
Chapter 7 EXTERNAL FORCED CONVECTION
Internal Flow: Heat Transfer Correlations. Fully Developed Flow Laminar Flow in a Circular Tube: The local Nusselt number is a constant throughout the.
Chapter 7 Natural convection systems. 7-1 Introduction  natural or free convection: the motion of the fluid due to density changes arising from heating.
HW/Tutorial # 1 WRF Chapters 14-15; WWWR Chapters ID Chapters 1-2 Tutorial #1 WRF#14.12, WWWR #15.26, WRF#14.1, WWWR#15.2, WWWR#15.3, WRF#15.1, WWWR.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 7 External flow.
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 9 Free Convection.
Chapter 7: External Forced Convection
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 8 Internal flow.
CHAPTER 6 Introduction to convection
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Internal Flow: Heat Transfer Correlations
Chapter 7 EXTERNAL FORCED CONVECTION
Heat Transfer External Convection.
Chapter 8: Internal Flow
HW/Tutorial # 1 WRF Chapters 14-15; WWWR Chapters ID Chapters 1-2
Chapter 8 : Natural Convection
Boundary Layer and separation
Fundamentals of Convection
Natural Convection New terms Volumetric thermal expansion coefficient
Heat Transfer Coefficient
Internal Flow: General Considerations
Chapter 19 FORCED CONVECTION
Chapter 19 FORCED CONVECTION
Heat Transfer Correlations for Internal Flow
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Presentation transcript:

Boundary Layer and separation Flow accelerates Flow decelerates Constant flow Flow reversal free shear layer highly unstable Separation point

Flow Separation Separation Boundary layer Wake Stagnation point  Inviscid curve Turbulent Laminar 

Drag Coefficient: C D Supercritical flow turbulent B.L. Stokes’ Flow, Re<1 Relatively constant C D

Local Heat Transfer Distribution  q  ”=h(  )(T s -T  ), Nu  =h(  )D/k f Local Nusselt number for airflow normal to a circular cylinder. (figure from the ITHT text) Stagnation point Laminar B.L. growth separation Laminar to turbulent transition Turbulent B.L. growth Turbulent separation

Averaged Nusselt Number Correlations of Cylinders in Cross Flows Note 1: averaged Nusselt number correlations for the circular cylinder flows can be found in chapter Correlations for other noncircular cylinders in cross flow can also be found in this chapter (see Table 10-3). Note 2: Heat transfer between a tube bank (tube bundle) and cross flow is given in many HT textbooks (for example: see chapter 7 of “Introduction to Heat Transfer” by Incropera & DeWitt. The configuration is important for many practical applications, for example, the multiple pass heat exchanger in a condenser unit. The use of tube bank can not only save the operating space but also can enhance heat transfer. The wake flows behind each row of tubes are highly turbulent and can greatly enhance the convective heat transfer. In general, one can find an averaged convection coefficient using empirical correlation. Note 3: Because of its compactness, pressure drop across a tube bank can be also significant and warrants careful design consideration.

Example A hot-wire anemometer is a flow device used to measure flow velocity based on the principle of convective heat transfer. Electric current is passing through a thin cylindrical wire to heat it up to a high temperature, that is why it is called “hot-wire”. Heat is dissipated to the fluid flowing the wire by convection heat transfer such that the wire can be maintained at a constant temperature. Determine the velocity of the airstream (it is known to be higher than 40 m/s and has a temperature of 25°C), if a wire of 0.02 mm diameter achieved a constant temperature of 150°C while dissipating 50 W per meter of electric energy. Hot-wire, 0.02 mm dia. Constant temperature 150°C 25°C, U>40 m/s Air (87.5°C), Pr=0.707, =15  m 2 /s, k=0.026 W/m.K

Example (cont.)