Chapter 2: Problem 41
Why do we try to avoid the radiation boundary conditions in heat transfer analysis?
Chapter 2: Problem 41
Why do we try to avoid the radiation boundary conditions in heat transfer analysis?
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Get started for freeConsider a third-order linear and homogeneous differential equation. How many arbitrary constants will its general solution involve?
Consider a large plane wall of thickness \(L=0.3 \mathrm{~m}\), thermal conductivity \(k=2.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=12 \mathrm{~m}^{2}\). The left side of the wall at \(x=0\) is subjected to a net heat flux of \(\dot{q}_{0}=700 \mathrm{~W} / \mathrm{m}^{2}\), while the temperature at that surface is measured to be $T_{1}=80^{\circ} \mathrm{C}$. Assuming constant thermal conductivity and no heat generation in the wall, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the wall, \((b)\) obtain a relation for the variation of temperature in the wall by solving the differential equation, and ( \(c\) ) evaluate the temperature of the right surface of the wall at \(x=L\). Answer: (c) \(-4^{\circ} \mathrm{C}\)
A long homogeneous resistance wire of radius \(r_{o}=5 \mathrm{~mm}\) is being used to heat the air in a room by the passage of electric current. Heat is generated in the wire uniformly at a rate of $5 \times 10^{7} \mathrm{~W} / \mathrm{m}^{3}$ as a result of resistance heating. If the temperature of the outer surface of the wire remains at \(180^{\circ} \mathrm{C}\), determine the temperature at \(r=3.5 \mathrm{~mm}\) after steady operation conditions are reached. Take the thermal conductivity of the wire to be $k=8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(. Answer: \)200^{\circ} \mathrm{C}$
The variation of temperature in a plane wall is determined to be $T(x)=110 x-48 x\( where \)x\( is in \)\mathrm{m}\( and \)T\( is in \){ }^{\circ} \mathrm{C}$. If the thickness of the wall is \(0.75 \mathrm{~m}\), the temperature difference between the inner and outer surfaces of the wall is (a) \(110^{\circ} \mathrm{C}\) (b) \(74^{\circ} \mathrm{C}\) (c) \(55^{\circ} \mathrm{C}\) (d) \(36^{\circ} \mathrm{C}\) (e) \(18^{\circ} \mathrm{C}\)
Consider a long rectangular bar of length \(a\) in the \(x\)-direction and width \(b\) in the \(y\)-direction that is initially at a uniform temperature of \(T_{i}\). The surfaces of the bar at \(x=0\) and \(y=0\) are insulated, while heat is lost from the other two surfaces by convection to the surrounding medium at temperature \(T_{\infty}\) with a heat transfer coefficient of \(h\). Assuming constant thermal conductivity and transient twodimensional heat transfer with no heat generation, express the mathematical formulation (the differential equation and the boundary and initial conditions) of this heat conduction problem. Do not solve.
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