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Consider a flat ceiling that is built around $38-\mathrm{mm} \times 90-\mathrm{mm}\( wood studs with a center-to-center distance of \)400 \mathrm{~mm}\(. The lower part of the ceiling is finished with \)13-\mathrm{mm}$ gypsum wallboard, while the upper part consists of a wood subfloor \(\left(R=0.166 \mathrm{~m}^{2},{ }^{\circ} \mathrm{C} / \mathrm{W}\right)\), a 13 -mm plywood layer, a layer of felt $\left(R=0.011 \mathrm{~m}^{2},{ }^{\circ} \mathrm{C} / \mathrm{W}\right)\(, and linoleum \)\left(R=0.009 \mathrm{~m}^{2},{ }^{\circ} \mathrm{C} / \mathrm{W}\right)$. Both sides of the ceiling are exposed to still air. The airspace constitutes 82 percent of the heat transmission area, while the studs and headers constitute 18 percent. Determine the winter \(R\)-value and the \(U\)-factor of the ceiling assuming the 90 -mm-wide airspace between the studs \((a)\) does not have any reflective surface, \((b)\) has a reflective surface with \(\varepsilon=0.05\) on one side, and \((c)\) has reflective surfaces with \(\varepsilon=0.05\) on both sides. Assume a mean temperature of \(10^{\circ} \mathrm{C}\) and a temperature difference of \(5.6^{\circ} \mathrm{C}\) for the airspace.

Short Answer

Expert verified
Answer: The R-value for the ceiling with reflective surfaces with an emissivity of 0.05 on both sides is 7.210 m²K/W, and the U-factor is 0.139 W/m²K.

Step by step solution

01

1. Calculate the R-value of individual layers

To find the R-value of the ceiling, we first need to find the R-value for individual layers: - Wood subfloor: \(R=0.166\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) - Gypsum wallboard: Thickness is 13 mm, we will need the thermal conductivity (\(k\)) of the wallboard to calculate the R-value. - Plywood: Thickness is 13 mm, we will need the thermal conductivity (\(k\)) of plywood to calculate the R-value. - Felt: \(R=0.011\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) - Linoleum: \(R=0.009\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) For the calculation, we assume the following thermal conductivity values: - Gypsum wallboard: \(k_{gw} = 0.17\,\mathrm{W}/\mathrm{m}\mathrm{}^{\circ}\mathrm{C}\) - Plywood: \(k_{p} = 0.13\,\mathrm{W}/\mathrm{m}\mathrm{}^{\circ}\mathrm{C}\) Using the formula for R-value, \(R=\frac{thickness}{k}\) - Gypsum wallboard: \(R_{gw}=\frac{0.013\,\mathrm{m}}{0.17\,\mathrm{W}/\mathrm{m}\mathrm{}^{\circ}\mathrm{C}} = 0.076\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) - Plywood: \(R_{p}=\frac{0.013\,\mathrm{}}{0.13\,\mathrm{W}/\mathrm{m}\mathrm{}^{\circ}\mathrm{C}} = 0.100\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) Now, we have the R-value for every layer.
02

2. Calculate the R-value of the airspace with different scenarios

To find the R-value of the airspace, we will analyze three different scenarios \((a)\), \((b)\), \((c)\) with different reflective surfaces: (a) No reflective surface: Without a reflective surface, the R-value of the airspace can be found using the formula: \(R_{air}=\frac{1}{k_{air}*velocity}\), where \(k_{air}\) is the thermal conductivity of air and velocity is the velocity of air. However, we need more information about the velocity of air in this scenario. (b) Reflective surface with \(\varepsilon=0.05\) on one side: Let's assume that the required emissivity is given by \(\varepsilon=0.05\), and the temperature difference across airspace is \(\Delta T=5.6\,\mathrm{}^{\circ}\mathrm{C}\). The formula for calculating the R-value of airspace with reflective surface on one side is given by: \(R_{air\,b}=\frac{1}{hr}=\frac{1}{\frac{\varepsilon\sigma(T_{mean}^{2}+T_{inside}^{2})(T_{mean}+T_{inside})}}\) For this formula, we need: - \(T_{mean}=10^{\circ} \mathrm{C}\) - \(\sigma = 5.67\cdot10^{-8}\, \mathrm{W}/\mathrm{m}^2\mathrm{K}^4\) Calculation: \(R_{air\,b} =\frac{1}{0.05\cdot5.67\cdot10^{-8}\cdot((10+273)^2+(10+5.6+273)^2)((10+273)+(10+5.6+273))} = 4.357\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) (c) Reflective surfaces with \(\varepsilon=0.05\) on both sides: For this scenario, we use this formula with two reflective surfaces: \(R_{air\,c}=\frac{1}{2hr}=\frac{1}{2\frac{\varepsilon\sigma(T_{mean}^{2}+T_{inside}^{2})(T_{mean}+T_{inside})}}\) Calculation: \(R_{air\,c}=\frac{1}{2\times0.05\times5.67\times10^{-8}\times((10+273)^2+(10+5.6+273)^2)((10+273)+(10+5.6+273))} = 8.713\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\)
03

3. Calculate the R-value and U-factor of the ceiling for each scenario

Finally, we will calculate the R-value and U-factor of the ceiling by considering the airspace constitutes 82% of the heat transmission area and the studs and headers constitute 18%. We will add the R-value of the layers to the R-value of the airspace obtained in each scenario and obtain the U-factor with the formula \(U = \frac{1}{R}\). (a) No reflective surface: Incomplete information. (b) Reflective surface with \(\varepsilon=0.05\) on one side: \(R_{total\,b}=0.82\cdot R_{air\,b}+ 0.18\cdot(R_{gw}+R_{wood\,sub}+R_{p}+R_{felt}+R_{lin})\) \(R_{total\,b}=0.82\cdot 4.357 + 0.18\cdot(0.076+0.166+0.100+0.011+0.009)= 3.573+0.065=3.638\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) Now, the U-factor: \(U_{total\,b}=\frac{1}{R_{total\,b}}= \frac{1}{3.638} = 0.275\,\mathrm{W}/\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}\) (c) Reflective surfaces with \(\varepsilon=0.05\) on both sides: \(R_{total\,c}=0.82\cdot R_{air\,c}+ 0.18\cdot(R_{gw}+R_{wood\,sub}+R_{p}+R_{felt}+R_{lin})\) \(R_{total\,c}=0.82\cdot 8.713 + 0.18\cdot(0.076+0.166+0.100+0.011+0.009) = 7.145+0.065 = 7.210\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) Now, the U-factor: \(U_{total\,c}=\frac{1}{R_{total\,c}}= \frac{1}{7.210} = 0.139\,\mathrm{W}/\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}\) The R-value and U-factor for each scenario are: - (b) Reflective surface with \(\varepsilon=0.05\) on one side: \(R_{total\,b} = 3.638\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) and \(U_{total\,b} = 0.275\,\mathrm{W}/\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}\). - (c) Reflective surfaces with \(\varepsilon=0.05\) on both sides: \(R_{total\,c} = 7.210\,\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}/\mathrm{W}\) and \(U_{total\,c} = 0.139\,\mathrm{W}/\mathrm{m}^{2}\mathrm{}^{\circ}\mathrm{C}\).

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Most popular questions from this chapter

Consider a wall that consists of two layers, \(A\) and \(B\), with the following values: $k_{A}=1.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, L_{A}=8 \mathrm{~cm}\(, \)k_{B}=0.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, L_{B}=5 \mathrm{~cm}\(. If the temperature drop across the wall is \)18^{\circ} \mathrm{C}$, the rate of heat transfer through the wall per unit area of the wall is (a) \(56.8 \mathrm{~W} / \mathrm{m}^{2}\) (b) \(72.1 \mathrm{~W} / \mathrm{m}^{2}\) (c) \(114 \mathrm{~W} / \mathrm{m}^{2}\) (d) \(201 \mathrm{~W} / \mathrm{m}^{2}\) (e) \(270 \mathrm{~W} / \mathrm{m}^{2}\)

Using a timer (or watch) and a thermometer, conduct this experiment to determine the rate of heat gain of your refrigerator. First, make sure that the door of the refrigerator is not opened for at least a few hours to make sure that steady operating conditions are established. Start the timer when the refrigerator stops running, and measure the time \(\Delta t_{1}\) it stays off before it kicks in. Then measure the time \(\Delta t_{2}\) it stays on. Noting that the heat removed during \(\Delta t_{2}\) is equal to the heat gain of the refrigerator during \(\Delta t_{1}+\Delta t_{2}\) and using the power consumed by the refrigerator when it is running, determine the average rate of heat gain for your refrigerator, in watts. Take the COP (coefficient of performance) of your refrigerator to be \(1.3\) if it is not available. Now, clean the condenser coils of the refrigerator and remove any obstacles in the way of airflow through the coils. Then determine the improvement in the COP of the refrigerator.

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.

A pipe is insulated such that the outer radius of the insulation is less than the critical radius. Now the insulation is taken off. Will the rate of heat transfer from the pipe increase or decrease for the same pipe surface temperature?

Hot liquid is flowing in a steel pipe with an inner diameter of $D_{1}=22 \mathrm{~mm}\( and an outer diameter of \)D_{2}=27 \mathrm{~mm}$. The inner surface of the pipe is coated with a thin fluorinated ethylene propylene (FEP) lining. The thermal conductivity of the pipe wall is $15 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. The pipe outer surface is subjected to a uniform flux of \(1200 \mathrm{~W} / \mathrm{m}^{2}\) for a length of \(1 \mathrm{~m}\). The hot liquid flowing inside the pipe has a mean temperature of $180^{\circ} \mathrm{C}\( and a convection heat transfer coefficient of \)50 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The interface between the FEP lining and the steel surface has a thermal contact conductance of $1500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Determine the temperatures at the lining and at the pipe outer surface for the pipe length subjected to the uniform heat flux. What is the total thermal resistance between the two temperatures? The ASME Code for Process Piping (ASME B31.3-2014, A.323) recommends a maximum temperature for FEP lining to be \(204^{\circ} \mathrm{C}\). Does the FEP lining comply with the recommendation of the code?

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