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Heat & Mass Transfer - acharya ng ranga agricultural university

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(In the derivations, the expression for the derivative at<br />

x + dx<br />

has been<br />

written in the form of a Taylor-Series expression with only the first two terms<br />

of the series employed for the development.)<br />

where<br />

.<br />

q = energy generated per unit volume, W /m 3<br />

c = specific heat of material, J /kg .°C<br />

ρ = density, kg/m 3<br />

Combining the relations above gives<br />

or<br />

heat source.<br />

∂<br />

− kA T<br />

+<br />

∂x<br />

q .<br />

Adx =<br />

∂T<br />

ρcA<br />

dx ∂τ<br />

⎡ ∂T<br />

− A⎢k<br />

⎣ ∂x<br />

.<br />

∂ ⎛ ∂T<br />

⎞ ∂T<br />

⎜k<br />

⎟dx<br />

+ q=ρc<br />

∂x<br />

⎝ ∂x<br />

⎠ ∂ τ<br />

∂ ⎛ ∂T<br />

⎞ ⎤<br />

+ ⎜k<br />

⎟dx<br />

∂x<br />

⎥<br />

⎝ ∂x<br />

⎠ ⎦<br />

This is the one-dimensional steady state heat-conduction equation with<br />

Figure 2.2 Elemental volume for three-dimensional heat-conduction analysis:<br />

(a) cartesian coordinates; (b) cylindrical coordinates;<br />

(c) spherical coordinates.

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