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Steam at \(260^{\circ} \mathrm{C}\) is flowing inside a steel pipe $(k=61 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ whose inner and outer diameters are \(10 \mathrm{~cm}\) and \(12 \mathrm{~cm}\), respectively, in an environment at \(20^{\circ} \mathrm{C}\). The heat transfer coefficients inside and outside the pipe are 120 \(\mathrm{W} / \mathrm{m}^{2}, \mathrm{~K}\) and $14 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\(, respectively. Determine \)(a)$ the thickness of the insulation $(k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( needed to reduce the heat loss by 95 percent and \)(b)$ the thickness of the insulation needed to reduce the exposed surface temperature of insulated pipe to \(40^{\circ} \mathrm{C}\) for safety reasons.

Short Answer

Expert verified
#Answer# The thickness of insulation needed to reduce the heat loss by 95% is found by solving the equation in Step 2: \(0.05 \cdot Q_{uninsulated} = U_{insulated} \cdot A_{s2} \cdot (T_s - T_{\infty})\) The thickness of insulation needed to have an exposed surface temperature of \(40^{\circ} \mathrm{C}\) is found by solving the equation in Step 3: \(40^{\circ} \mathrm{C} = T_s - \frac{Q_{insulated}}{U_{insulated} \cdot A_{s2}}\) The exact values for the thickness in both cases would depend on the specific parameters provided, such as the properties of the pipe, insulation, and environment.

Step by step solution

01

Calculate the Heat Loss of Uninsulated Pipe

First, we need to determine the heat loss of the uninsulated pipe. We can use the following formula for the overall heat transfer coefficient of the uninsulated pipe: \(U_{uninsulated} = \frac{1}{\frac{1}{h_i} + \frac{\ln(r_o/r_i)}{2 \pi k L} + \frac{1}{h_o}}\) Where \(h_i\) and \(h_o\) are inside and outside heat transfer coefficients, \(r_i\) and \(r_o\) are inside and outside radii of the pipe, \(k\) is the thermal conductivity of steel, and \(L\) is the length of the pipe. Now we can calculate the heat loss (\(Q_{uninsulated}\)) of the uninsulated pipe using the formula: \(Q_{uninsulated} = U_{uninsulated} \cdot A_s \cdot (T_s - T_{\infty})\) Where \(A_s=2 \pi r_o L\) is the surface area of the pipe, \(T_s\) is the steam temperature, and \(T_{\infty}\) is the environment temperature.
02

Determine the Insulation Thickness for 95% Heat Loss Reduction

Now, we want to find the thickness of insulation (\(t\)) needed to reduce the heat loss by 95%. So, the heat loss of the insulated pipe should be 5% of the uninsulated pipe heat loss: \(Q_{insulated} = 0.05 \cdot Q_{uninsulated}\) We can use the formula for the overall heat transfer coefficient of the insulated pipe: \(U_{insulated} = \frac{1}{\frac{1}{h_i} + \frac{\ln(r_o/r_i)}{2 \pi k L}+\frac{\ln(r_2/r_o)}{2 \pi k_{ins} L} + \frac{1}{h_o}}\) Where \(k_{ins}\) is the thermal conductivity of insulation material, and \(r_2\) is the outer radius of the insulation. Note that \(t = r_2 - r_o\). Now we can calculate the heat loss (\(Q_{insulated}\)) of the insulated pipe using the formula: \(Q_{insulated} = U_{insulated} \cdot A_{s2} \cdot (T_s - T_{\infty})\) Where \(A_{s2} = 2 \pi r_2 L\) is the outer surface area of the insulation. Use this equation to solve for the insulation thickness (\(t\)): \(0.05 \cdot Q_{uninsulated} = U_{insulated} \cdot A_{s2} \cdot (T_s - T_{\infty})\)
03

Determine the Insulation Thickness for 40C Exposed Surface Temperature

We can use the relationship for the outer surface temperature (\(T_{s2}\)) of the insulation: \(T_{s2} = T_s - \frac{Q_{insulated}}{U_{insulated} \cdot A_{s2}}\) We want to find the insulation thickness (\(t\)) needed to have an exposed surface temperature of \(40^{\circ} \mathrm{C}\). We can write an equation for \(T_{s2} = 40^{\circ} \mathrm{C}\) and use it to solve for \(t\): \(40^{\circ} \mathrm{C} = T_s - \frac{Q_{insulated}}{U_{insulated} \cdot A_{s2}}\) After solving the equations in Steps 2 and 3, we will get the thickness of the insulation needed for both cases, giving us the final answers.

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Most popular questions from this chapter

Liquid flows in a metal pipe with an inner diame\(D_{2}=32\) ter of $D_{1}=22 \mathrm{~mm}\( and an outer diameter of \)D_{2}=32 \mathrm{~mm}$. The thermal conductivity of the pipe wall is $12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The inner surface of the pipe is coated with a thin polyvinylidene chloride (PVDC) lining. Along a length of \(1 \mathrm{~m}\), the pipe outer surface is exposed to convection heat transfer with hot gas, at \(T_{\infty}=100^{\circ} \mathrm{C}\) and $h=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(, and thermal radiation with a surrounding at \)T_{\text {surr }}=100^{\circ} \mathrm{C}\(. The emissivity at the pipe outer surface is \)0.3$. The liquid flowing inside the pipe has a convection heat transfer coefficient of \(50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the outer surface of the pipe is at \(85^{\circ} \mathrm{C}\), determine the temperature at the PVDC lining and the temperature of the liquid. The ASME Code for Process Piping (ASME B31.3-2014, A.323) recommends a maximum temperature for PVDC lining to be \(79^{\circ} \mathrm{C}\). Does the PVDC lining comply with the recommendation of the code?

A \(2.5\)-m-high, 4-m-wide, and 20 -cm-thick wall of a house has a thermal resistance of \(0.025^{\circ} \mathrm{C} / \mathrm{W}\). The thermal conductivity of the wall is (a) \(0.8 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (b) \(1.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (c) \(3.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (d) \(5.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (e) \(8.0 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\)

A 1-cm-diameter, 30-cm-long fin made of aluminum $(k=237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( is attached to a surface at \)80^{\circ} \mathrm{C}\(. The surface is exposed to ambient air at \)22^{\circ} \mathrm{C}$ with a heat transfer coefficient of $18 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. If the fin can be assumed to be very long, the rate of heat transfer from the fin is (a) \(2.0 \mathrm{~W}\) (b) \(3.2 \mathrm{~W}\) (c) \(4.4 \mathrm{~W}\) (d) \(5.5 \mathrm{~W}\) (e) \(6.0 \mathrm{~W}\)

The heat transfer surface area of a fin is equal to the sum of all surfaces of the fin exposed to the surrounding medium, including the surface area of the fin tip. Under what conditions can we neglect heat transfer from the fin tip?

A 10-m-long, 8-cm-outer-radius cylindrical steam pipe is covered with 3 -cm- thick cylindrical insulation with a thermal conductivity of $0.05 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. If the rate of heat loss from the pipe is \(1000 \mathrm{~W}\), the temperature drop across the insulation is (a) \(58^{\circ} \mathrm{C}\) (b) \(101^{\circ} \mathrm{C}\) (c) \(143^{\circ} \mathrm{C}\) (d) \(282^{\circ} \mathrm{C}\) (e) \(600^{\circ} \mathrm{C}\)

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