Chapter (3) Conduction · Conduction Conduction with Thermal Energy Generation Radial Systems...

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Conduction 11/24/2015 Dr. Ismail Mahmoud Metwally El_Semary 1 Chapter ( 3 )

Transcript of Chapter (3) Conduction · Conduction Conduction with Thermal Energy Generation Radial Systems...

  • Conduction

    11/24/2015 Dr. Ismail Mahmoud Metwally El_Semary 1

    Chapter (3)

  • 11/24/2015 Dr. Ismail Mahmoud Metwally El_Semary 2

    Chapter (3)

    Conduction

    By the end of today’s lecture, you should be able to:

    Learn how to deal with heat generation problems.

    Learn how to treat the extended surfaces (fins)

    Goals:

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    Chapter (3)

    Conduction

    Conduction with Thermal

    Energy Generation

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    Conduction

    Conduction with Thermal

    Energy Generation

    Plan Wall

    Chapter (3)

    Consider situations for which thermal energy is being Generated,

    as in chemical reactions, electrical energy, nuclear energy

    Assumptions

    The energy generation is uniform per unit volume 𝑞. = 𝐶𝑜𝑛𝑠𝑡. Steady state.

    One dimension

    Constant thermal conductivity

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    Conduction

    Conduction with Thermal

    Energy Generation

    Plan Wall

    Chapter (3)

    From the general equation:

    Apply the previews assumptions

    Solution of the differential equation

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    Conduction

    Conduction with Thermal

    Energy Generation

    Plan Wall

    Chapter (3)

    Boundary conditions. . .

    Temperature distribution. . .

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    Conduction

    Conduction with Thermal

    Energy Generation

    Plan Wall

    Chapter (3)

    Cases of Heat Generation……

    Both the Sides at the Same

    Temperature

    Two Sides at Different

    Temperatures

    One Face Perfectly

    Insulated

    Plane Slab with Uniform Internal Heat Generation

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    Conduction

    Conduction with Thermal

    Energy Generation

    Plan Wall

    Chapter (3)

    Relationship between surface temperature and environmental temperature

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    Conduction

    Conduction with Thermal

    Energy Generation

    Radial Systems

    Chapter (3)

    Consider a simple case of one-dimensional conduction with heat generation

    in a pipe with the following assumptions:

    The energy generation is uniform per unit

    volume 𝑞. = 𝐶𝑜𝑛𝑠𝑡. Steady state.

    One dimension

    Constant thermal conductivity

  • 11/24/2015 Dr. Ismail Mahmoud Metwally El_Semary 10

    Conduction

    Conduction with Thermal

    Energy Generation Chapter (3)

    Radial Systems

    From the general equation:

    Apply the previews assumptions

    Solution of the differential equation

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    Conduction

    Conduction with Thermal

    Energy Generation Chapter (3)

    Radial Systems

    Boundary conditions. . .

    Temperature distribution. . .

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    Conduction

    Chapter (3)

    Heat Transfer From External

    Surface (Fins)

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Fin Purposes and Applications

    Fins are extended surfaces that are utilized in the removal of heat from a

    body

    One can increase heat transfer by increasing the heat transfer coefficient or

    increasing the surface area

    Finned surfaces are manufactured by extruding, welding, or wrapping a

    thin metal sheet on a surface

    Fins are often seen in electrical appliance such as in computer power

    supply cooling or substation transformers and are also used for engine

    cooling such as car radiators

    Example

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Many designs are possible, where Fin designs are only limited by

    imagination:

    (a) Straight fin of uniform cross-section

    (b) Straight fin non-uniform cross-section

    (c) Annular fin

    (d) Pin fin

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    How fins work

    Fins enhance heat transfer from a surface by exposing a larger

    surface area to convection and radiation

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Fin Equation

    Assumptions:

    Steady state.

    One dimension

    Constant thermal conductivity

    No heat generation

    Uniform cross section area

    T∞ = temp. of surrounding

    Tb = fin temp. at base

    A = cross-sectional area of fin

    P = perimeter of fin

    L = fin length

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Fin Equation

    For the differential Element shown; The heat balance equation is:

    Or

    Where

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Substituting and dividing by ∆x, we obtain

    Taking the limit as ∆x → 0 gives

    Where

    Fin Equation

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Integrate the equation

    The general solution to this differential equation is:

    From the boundary conditions:

    1st boundary condition: Boundary condition at fin base

    2nd boundary condition: At X = L different conditions are possible

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    CASE I. Infinitely Long Fin (T fin tip =T ∞)

    Assume a very long fin, L approaches infinity. Thus, the temperature at the

    end of the fin should be practically equal to the temperature of the

    surrounding fluid. Then;

    Substitute in the previous equation:

    Determination of C1 and C2 leads to,

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    The Temperature Distribution:

    The Heat Transfer Rate:

    Where: P is the perimeter, Ac is the cross-sectional area of the fin,

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    CASE II. Negligible Heat Loss from the Fin Tip (Insulated fin tip, Q fin tip = 0)

    The fin has a finite length, L, and the end is insulated, which means that:

    The Temperature Distribution:

    The Heat Transfer Rate:

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    CASE III. Convection (or Combined Convection and Radiation) from Fin Tip

    The fin has a finite length, L, and losses heat by convection from its end

    The Temperature Distribution:

    The Heat Transfer Rate:

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Corrected length

    CASE III. Convection (or Combined Convection and Radiation) from Fin Tip

    A practical way of accounting for the heat

    loss from the fin tip is to replace the fin

    length L in the relation for the insulated tip

    case by a Defined length as:

    Where:

    t is the thickness of the rectangular fins and

    D is the diameter of the cylindrical fins.

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Fin Efficiency

    The maximum heat loss through convection will

    be when the driving force (i.e. temperature

    difference between the base and fluid) remains

    the same at all points along the fin.

    A definition of the fin efficiency is therefore

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Fin Efficiency

    Fin efficiency relations are developed for fins of various profiles and are

    plotted charts as shown in the following charts.

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    Conduction

    Chapter (3) Heat Transfer From External Surface (Fins)

    Fin Effectiveness

    Fins are used to enhance heat transfer, and the use of fins on a surface cannot be

    recommended unless the enhancement in heat transfer justifies the added cost

    and complexity associated with the fins. In fact, there is no assurance that adding

    fins on a surface will enhance heat transfer. The performance of the fins is

    judged on the basis of the enhancement in heat transfer relative to the no-fin

    case. The performance of fins expressed in terms of the fin effectiveness , εfin is

    defined as: