Experiment 2

Extended Surface Heat Transfer

Download  Experiment Description


Objectives
Theoretical Background
Apparatus
Experimental Procedure
Question to be Answered
Download Data Sheet
Related Notes(EML3016)
Supplemental Notes on Convective Heat Transfer
Picture

Objectives

To examine the heat transfer in a single cylindrical extended surface (a fin or a pin) in free or forced convection. To develop an understanding of fin effectiveness and the parameters which influence it.

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Theoretical Background
( For more detailed discussion, go to EML 3016  Notes )

An extended surface is commonly used in reference to a solid that experiences energy transfer by conduction within its boundaries, as well as energy transfer by convection between its boundaries and its surroundings. The extended surface is most often utilized in the removal of heat from a body. In this case, the extended surface is often referred to as a ``fin''. A fin with a cylindrical shape and a high aspect ratio (length/diameter) is called a pin. Fins are often seen in electrical appliance cooling such as in a computer power supply or substation transformers. Fins are also used for engine cooling. Figure 1 illustrates different fin shapes. The analysis of fin heat
 
 


 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 
 

Figure 1. Various extended surfaces












transfer assuming steady state, one-dimensional heat conduction (temperature varies only axially and not radially), uniform convective heat transfer coefficient, h, and constant thermal conductivity, k, results in the differential heat equation in the following form,
 
 


                                  (1)















where Ac is the cross-sectional area, As is the surface area, T is the temperature, and T¥ is the freestream temperature. If the fin has a uniform cross-sectional area, Ac, and a base temperature of Tb, Equation 1 reduces to
 
 


                                           (2)














where P is the perimeter. Defining
 
 

                                                                (3)














we can rewrite Equation 2 as

                                                                (4)

where m2 = h P/(k Ac). Equation 4 is a linear, homogeneous, 2nd order, constant coefficient ordinary differential equation, whose solutions depend on the boundary conditions.  A summary of various boundary conditions and the resulting solutions are given in Table 1. The effectiveness of an infinite fin is given by

                                                                       (5)

The fin effectiveness is defined as the ratio of the fin heat transfer rate to the heat transfer rate that would exist without the fin. It is often desired to maximize the fin effectiveness. There are various ways to achieve this.

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Apparatus

The following apparatus will be used in this experiment:

    1. A constant temperature bath.
    2. An extended surface constructed from aluminium, and shown in Figure 2.
    3. Thermocouples.
    4. Digital temperature indicator.
    5. Switchbox.
    6. Wind tunnel
Click here to see apparatus
 
 

Figure 2. Cylindrical extended surface, including thermocouple locations



 
 
 
 
 
 
 
 
 
 
 
 
 

Case Tip Condition
(x = L)
Temperature Distribution
Fin Heat Transfer Rate
A
 
 




B
 
 
 
 
 

C
 
 
 
 

D

Convection


 
 

Adiabatic


 
 

Prescribed Temp.


 
 

Infinite fin 


 
 


 
 


 
 
 
 


 
 
 


 
 


 
 
 
 
 

Table 1. Solutions to fin equation

Click here to see apparatus

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Experimental Procedure

    1. The constant temperature bath is adjusted to 80 ° C and started up at least an hour before the start of the lab session.
    2. Measure the free convection temperature profile, i.e. with the wind tunnel switched off.
    3. Record this temperature profile.
    4. Start the wind tunnel with the frequency set at 5 Hz.
    5. Allow the fin to reach steady state.
    6. Record the temperature profile.
    7. Repeat Steps 5- 6 for the wind tunnel counter settings of 5 - 40, in increments of 5.
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Question to be Answered

        1.      Calculate the non-dimensional temperature profile
 
 














               for each flow situation and compare it to the theoretical temperature profile.

        2.    Plot the nondimensional experimental and theoretical temperature profiles on the same graph for
               each flow situation.

        3.    Discuss the results in detail. Compare the experimental and theoretical values. What boundary
               conditions did you assume? Why? What may cause the experimental profile to differ from the
               theoretical profile?

        4.    Calculate the fin effectiveness. Which case has the highest effectiveness and why? Discuss ways
               to improve fin effectiveness.

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Experiment 2 Data Sheet

Note: Please note the units of the quantities which are being measured, when recording data. For example, when measuring voltage, if the voltmeter reads 16 mV, then write down 16 mV instead of just 16.

       1. Maintain constant temperature bath at approximately 80 oC.

        2. For each measurement allow fin to reach steady state then record the temperature profile. For
            steady state, wait 15 minutes after raising speed in windtunnel.

        3. Velocity (m/s)= 0.9523 (counter reading) - 1.4093 (calibration chart)
         
         
 
 

Frequency Reading
Tb
T1
T2
T3
T4
T5
T6
T7
T(inf)
0









5









10









15









-









40


























YOU NEED TO GET THE LAB INSTRUCTOR'S SIGNATURE BEFORE LEAVING.

The student has performed the experiment satisfactorily and has cleaned the work area.
 
 

___________________________ _______________

(Lab assistant's signature)                            Date

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