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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) \(18^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: The temperature difference between the inner and outer surfaces of the wall is \(74^{\circ} \mathrm{C}\).

Step by step solution

01

Calculate temperature at inner surface (x=0)

To calculate the temperature at the inner surface, we have to plug x = 0 in the given function: \(T(0) = 110(0) - 48(0)^2 = 0^{\circ} \mathrm{C}\)
02

Calculate temperature at outer surface (x=0.75)

To calculate the temperature at the outer surface, we have to plug x = 0.75 into the given function: \(T(0.75) = 110(0.75) - 48(0.75)^2= 74^{\circ} \mathrm{C}\)
03

Calculate the temperature difference

Now we can calculate the temperature difference between the inner and outer surfaces by subtracting inner surface temperature from the outer surface temperature: \(\Delta T = T(0.75) - T(0) = 74^{\circ} \mathrm{C} - 0^{\circ} \mathrm{C} = 74^{\circ} \mathrm{C}\) The temperature difference between the inner and outer surfaces of the wall is \(74^{\circ} \mathrm{C}\), so the correct answer is (b).

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Most popular questions from this chapter

What is heat generation? Give some examples.

Consider a steam pipe of length \(L=35 \mathrm{ft}\), inner radius $r_{1}=2 \mathrm{in}\(, outer radius \)r_{2}=24\( in, and thermal conductivity \)k=8 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}{ }^{\circ} \mathrm{F}$. Steam is flowing through the pipe at an average temperature of $250^{\circ} \mathrm{F}$, and the average convection heat transfer coefficient on the inner surface is given to be $h=15 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2},{ }^{\circ} \mathrm{F}$. If the average temperature on the outer surfaces of the pipe is \(T_{2}=160^{\circ} \mathrm{F},(a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the pipe, \((b)\) obtain a relation for the variation of temperature in the pipe by solving the differential equation, and (c) evaluate the rate of heat loss from the steam through the pipe.

Heat is generated in a long \(0.3-\mathrm{cm}\)-diameter cylindrical electric heater at a rate of \(150 \mathrm{~W} / \mathrm{m}^{3}\). The heat flux at the surface of the heater in steady operation is (a) \(42.7 \mathrm{~W} / \mathrm{cm}^{2}\) (b) \(159 \mathrm{~W} / \mathrm{cm}^{2}\) (c) \(150 \mathrm{~W} / \mathrm{cm}^{2}\) (d) \(10.6 \mathrm{~W} / \mathrm{cm}^{2}\) (e) \(11.3 \mathrm{~W} / \mathrm{cm}^{2}\)

A long electrical resistance wire of radius \(r_{1}=0.25 \mathrm{~cm}\) has a thermal conductivity $k_{\text {wirc }}=15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Heat is generated uniformly in the wire as a result of resistance heating at a constant rate of \(0.5 \mathrm{~W} / \mathrm{cm}^{3}\). The wire is covered with polyethylene insulation with a thickness of \(0.25 \mathrm{~cm}\) and thermal conductivity of $k_{\text {ins }}=0.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The outer surface of the insulation is subjected to free convection in air at \(20^{\circ} \mathrm{C}\) and a convection heat transfer coefficient of \(2 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Formulate the temperature profiles for the wire and the polyethylene insulation. Use the temperature profiles to determine the temperature at the interface of the wire and the insulation and the temperature at the center of the wire. The ASTM D1351 standard specifies that thermoplastic polyethylene insulation is suitable for use on electrical wire that operates at temperatures up to \(75^{\circ} \mathrm{C}\). Under these conditions, does the polyethylene insulation for the wire meet the ASTM D1351 standard?

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