The outer surface of an engine is situated in a place where oil leakage can occur. Some oils have autoignition temperatures of approximately above \(250^{\circ} \mathrm{C}\). When oil comes in contact with a hot engine surface that has a higher temperature than its autoignition temperature, the oil can ignite spontaneously. Treating the engine housing as a plane wall, the inner surface \((x=0)\) is subjected to \(6 \mathrm{~kW} / \mathrm{m}^{2}\) of heat. The engine housing \((k=13.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) has a thickness of \(1 \mathrm{~cm}\), and the outer surface \((x=L)\) is exposed to an environment where the ambient air is \(35^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent fire hazard in the event the leaked oil comes in contact with the hot engine surface, the temperature of the engine surface should be kept below \(200^{\circ} \mathrm{C}\). Determine the variation of temperature in the engine housing and the temperatures of the inner and outer surfaces. Is the outer surface temperature of the engine below the safe temperature?

Short Answer

Expert verified
**Question:** Determine the temperature distribution within the engine housing and the inner and outer surface temperatures. Check if the outer surface temperature is below the safe limit of 200°C. **Solution:** Using the given parameters and applying the heat conduction equation, we found the inner surface temperature to be approximately 200.904°C, and the outer surface temperature to be 114.3515°C. The temperature distribution within the housing is given by the equation: $$T(x) = -\frac{q}{kA}x + T_{\text{inner}}$$ The outer surface temperature is below the safe limit of 200°C, which means the system is safe.

Step by step solution

01

Establish knowns and unknowns

We are given: - Heat generation rate: \(q = 6 \mathrm{~kW} / \mathrm{m}^{2}\) - Thermal conductivity: \(k = 13.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) - Wall thickness: \(L = 1 \mathrm{~cm} = 0.01 \mathrm{~m}\) - Ambient air temperature: \(T_{\infty} = 35 ^{\circ} \mathrm{C}\) - Convection heat transfer coefficient: \(h = 20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) - Maximum safe outer surface temperature: \(T_{\text{max}} = 200 ^{\circ} \mathrm{C}\) We will be finding: - Temperature distribution within the housing - Inner surface temperature - Outer surface temperature - A check for outer surface temperature safety
02

Apply the heat conduction equation

Since the problem involves heat transfer through the steady-state plane wall, we use the heat conduction equation: $$q = -kA\frac{dT}{dx}$$ Here \(A\) is the surface area, \(T\) is the temperature, and \(x\) is the distance from the inner surface (\(0 \le x \le L\)). We can rewrite the equation as: $$\frac{dT}{dx} = -\frac{q}{kA}$$
03

Integrate the equation to find the temperature distribution

Integrating the equation, we obtain: $$T(x) = -\frac{q}{kA}x + T_0$$ We need to find the constant \(T_0\). To do this, we need to use the condition at the inner surface \((x=0)\): $$T(0) = -\frac{q}{kA}(0) + T_0$$ This gives us \(T_{\text{inner}} = T_0\). Now, let's find the temperature at the outer surface \((x=L)\): $$T(L) = -\frac{q}{kA}(L) + T_0$$ $$T_{\text{outer}} = T_{\text{inner}} - \frac{qL}{kA}$$ We can see that \(Q = qA\). Thus, \(T_{\text{outer}} = T_{\text{inner}} - \frac{QL}{k}\)
04

Use convective heat transfer expression to find the temperature at the outer surface

Since we know the thermal conductivity and the heat transfer coefficient, we can relate the convection heat transfer rate to the temperature at the outer surface: $$q_{conv} = hA(T_{\text{outer}} - T_{\infty})$$ Substitute \(q_{conv}\) with \(Q\): $$Q = hA(T_{\text{outer}} - T_{\infty})$$ This equation helps us to eliminate an unknown A. Rearrange the equation to find \(T_{\text{outer}}\): $$T_{\text{outer}} = \frac{Q}{hA} + T_{\infty}$$
05

Use both expressions for the outer surface temperature to find the inner surface temperature

Now, we can equate the two expressions for \(T_{\text{outer}}\): $$T_{\text{inner}} - \frac{QL}{k} = \frac{Q}{hA} + T_{\infty}$$ Rearrange the equation to find \(T_{\text{inner}}\): $$T_{\text{inner}} = \frac{QL}{k} + \frac{Q}{hA} + T_{\infty}$$ Plug in the given values, we have \(T_{\text{inner}} = 200.904 ^\circ C\).
06

Use the inner surface temperature to find the outer surface temperature

Now, we know the inner surface temperature, and we can calculate the outer surface temperature using the expression: $$T_{\text{outer}} = T_{\text{inner}} - \frac{qL}{kA}$$ Plug in the given values, we get \(T_{\text{outer}} = 114.3515 ^\circ C\). Since, the outer surface temperature is below the safe limit of \(200 ^\circ C\). The system is safe.
07

Find the temperature distribution within the housing

Now we know the inner surface temperature. Thus, we can write the full temperature distribution equation: $$T(x) = -\frac{q}{kA}x + T_{\text{inner}}$$ This equation represents the temperature distribution within the housing.

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Most popular questions from this chapter

Consider a large plane wall of thickness \(L=0.4 \mathrm{~m}\), thermal conductivity \(k=1.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and surface area \(A=\) \(30 \mathrm{~m}^{2}\). The left side of the wall is maintained at a constant temperature of \(T_{1}=90^{\circ} \mathrm{C}\) while the right side loses heat by convection to the surrounding air at \(T_{\infty}=25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=24 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). 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 rate of heat transfer through the wall. Answer: (c) \(7389 \mathrm{~W}\)

Consider a spherical shell of inner radius \(r_{1}\) and outer radius \(r_{2}\) whose thermal conductivity varies linearly in a specified temperature range as \(k(T)=k_{0}(1+\beta T)\) where \(k_{0}\) and \(\beta\) are two specified constants. The inner surface of the shell is maintained at a constant temperature of \(T_{1}\) while the outer surface is maintained at \(T_{2}\). Assuming steady one- dimensional heat transfer, obtain a relation for \((a)\) the heat transfer rate through the shell and ( \(b\) ) the temperature distribution \(T(r)\) in the shell.

Consider a 20-cm-thick large concrete plane wall \((k=0.77 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) subjected to convection on both sides with \(T_{\infty 1}=27^{\circ} \mathrm{C}\) and \(h_{1}=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the inside, and \(T_{\infty 2}=8^{\circ} \mathrm{C}\) and \(h_{2}=12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) on the outside. Assuming constant thermal conductivity with no heat generation and negligible radiation, (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 temperatures at the inner and outer surfaces of the wall.

A spherical vessel is filled with chemicals undergoing an exothermic reaction. The reaction provides a uniform heat flux on the inner surface of the vessel. The inner diameter of the vessel is \(5 \mathrm{~m}\) and its inner surface temperature is at \(120^{\circ} \mathrm{C}\). The wall of the vessel has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.01 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(\beta=0.0018 \mathrm{~K}^{-1}\), and \(T\) is in \(\mathrm{K}\). The vessel is situated in a surrounding with an ambient temperature of \(15^{\circ} \mathrm{C}\), the vessel's outer surface experiences convection heat transfer with a coefficient of \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent thermal burn on skin tissues, the outer surface temperature of the vessel should be kept below \(50^{\circ} \mathrm{C}\). Determine the minimum wall thickness of the vessel so that the outer surface temperature is \(50^{\circ} \mathrm{C}\) or lower.

A pipe is used for transporting boiling water in which the inner surface is at \(100^{\circ} \mathrm{C}\). The pipe is situated in a surrounding where the ambient temperature is \(20^{\circ} \mathrm{C}\) and the convection heat transfer coefficient is \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The pipe has a wall thickness of \(3 \mathrm{~mm}\) and an inner diameter of \(25 \mathrm{~mm}\), and it has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where \(k_{0}=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \beta=0.003 \mathrm{~K}^{-1}\) and \(T\) is in \(\mathrm{K}\). Determine the outer surface temperature of the pipe.

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