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Consider a \(1.5\)-m-high electric hot-water heater that has a diameter of $40 \mathrm{~cm}\( and maintains the hot water at \)60^{\circ} \mathrm{C}$. The tank is located in a small room whose average temperature is $27^{\circ} \mathrm{C}$, and the heat transfer coefficients on the inner and outer surfaces of the heater are 50 and $12 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, respectively. The tank is placed in another \(46-\mathrm{cm}\)-diameter sheet metal tank of negligible thickness, and the space between the two tanks is filled with foam insulation $(k=0.03 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. The thermal resistances of the water tank and the outer thin sheet metal shell are very small and can be neglected. The price of electricity is \(\$ 0.08 / \mathrm{kWh}\), and the homeowner pays \(\$ 280\) a year for water heating. Determine the fraction of the hot-water energy cost of this household that is due to the heat loss from the tank. Hot-water tank insulation kits consisting of 3 -cm-thick fiberglass insulation \((k=0.035 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) large enough to wrap the entire tank are available in the market for about \(\$ 30\). If such an insulation is installed on this water tank by the homeowner himself, how long will it take for this additional insulation to pay for itself?

Short Answer

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Now, we can calculate the heat loss rate: $$ \dot{Q} = \frac{5 \cdot 1.885 (80 - 20)}{(5/10)(1.885/2.670) + (1)} $$ #tag_title#Step 2: Calculate the cost of heat loss per year and the fraction of total hot-water energy cost#tag_content#To find the cost of heat loss per year, we multiply the heat loss rate by the number of hours in a year and the cost of electricity: $$ \text{Cost per year} = \dot{Q} \cdot \text{Hours per year} \cdot \text{Cost of electricity} $$ The fraction of total hot-water energy cost can be calculated using the following formula: $$ \text{Fraction of hot-water energy cost} = \frac{\text{Cost of heat loss per year}}{\text{Total hot-water energy cost per year}} $$ #tag_title#Step 3: Determine the new heat loss rate after installing the additional insulation layer#tag_content#After installing the additional insulation layer, we need to calculate the new heat loss rate. We first need to calculate the new thermal resistance of insulation: $$ R_{new\ insulation} = R_{insulation} + \frac{L_{additional}}{k_{additional}} $$ Next, we can calculate the new heat loss rate using the same formula as in Step 1, but with the updated \(R_{new\ insulation}\). $$ \dot{Q}_{new} = \frac{h_{i} A_{i}(T_{s}- T_{w})}{(h_{i}/h_{o})(A_{i}/A_{o}) + (R_{new\ insulation})} $$ #tag_title#Step 4: Calculate the payback time for the insulation kit#tag_content#To calculate the payback time, we first need to determine the annual energy savings: $$ \text{Annual energy savings} = (\dot{Q} - \dot{Q}_{new}) \cdot \text{Hours per year} \cdot \text{Cost of electricity} $$ Next, we can find the payback time by dividing the insulation kit's initial cost by the annual energy savings: $$ \text{Payback time} = \frac{\text{Initial cost of insulation kit}}{\text{Annual energy savings}} $$ Finally, the payback time is calculated, and we can determine whether the insulation kit is worth the investment.

Step by step solution

01

Calculate the heat loss rate from the tank without insulation kit

First, we need to find the heat loss rate from the tank without an insulation kit. We can use the formula for the heat loss rate through a cylindrical wall: $$ \dot{Q} = \frac{h_{i} A_{i}(T_{s}- T_{w})}{(h_{i}/h_{o})(A_{i}/A_{o}) + (R_{insulation})} $$ Where, \(\dot{Q}\) is the heat loss rate (W) \(h_{i}\) and \(h_{o}\) are the inner and outer heat transfer coefficients (\(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\)) \(A_{i}\) and \(A_{o}\) are the inner and outer surface areas of the tank (m²) \(T_{s}\) and \(T_{w}\) are the tank surface and room temperatures (°C) \(R_{insulation}\) is the thermal resistance of insulation (m²·K/W) First, we calculate the inner and outer surface areas of the tank: $$A_{i} = 2 \pi r_{i} h = 2 \pi (0.2 \text{ m})(1.5 \text{ m})$$ $$A_{o} = 2 \pi r_{o} h = 2 \pi (0.23 \text{ m})(1.5 \text{ m})$$ Next, we find the thermal resistance of insulation: $$R_{insulation} = \frac{L}{k} = \frac{0.03}{0.03}$$

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Most popular questions from this chapter

A room at \(20^{\circ} \mathrm{C}\) air temperature is losing heat to the outdoor air at \(0^{\circ} \mathrm{C}\) at a rate of \(1000 \mathrm{~W}\) through a \(2.5\)-m-high and 4-m-long wall. Now the wall is insulated with \(2-\mathrm{cm}\)-thick insulation with a conductivity of $0.02 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Determine the rate of heat loss from the room through this wall after insulation. Assume the heat transfer coefficients on the inner and outer surfaces of the wall, the room air temperature, and the outdoor air temperature remain unchanged. Also, disregard radiation. (a) \(20 \mathrm{~W}\) (b) \(561 \mathrm{~W}\) (c) \(388 \mathrm{~W}\) (d) \(167 \mathrm{~W}\) (e) \(200 \mathrm{~W}\)

A 1-m-inner-diameter liquid-oxygen storage tank at a hospital keeps the liquid oxygen at \(90 \mathrm{~K}\). The tank consists of a \(0.5\)-cm-thick aluminum \((k=170 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) shell whose exterior is covered with a 10 -cm-thick layer of insulation \((k=0.02\) $\mathrm{W} / \mathrm{m} \cdot \mathrm{K})$. The insulation is exposed to the ambient air at \(20^{\circ} \mathrm{C}\). and the heat transfer coefficient on the exterior side of the insulation is \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The temperature of the exterior surface of the insulation is (a) \(13^{\circ} \mathrm{C}\) (b) \(9^{\circ} \mathrm{C}\) (c) \(2^{\circ} \mathrm{C}\) \((d)-3^{\circ} \mathrm{C}\) \((e)-12^{\circ} \mathrm{C}\)

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?

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?

Hot water at an average temperature of \(90^{\circ} \mathrm{C}\) is flowing through a \(15-\mathrm{m}\) section of a cast iron pipe $(k=52 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( whose inner and outer diameters are \)4 \mathrm{~cm}\( and \)4.6 \mathrm{~cm}$, respectively. The outer surface of the pipe, whose emissivity is \(0.7\), is exposed to the cold air at $10^{\circ} \mathrm{C}\( in the basement, with a heat transfer coefficient of \)15 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. The heat transfer coefficient at the inner surface of the pipe is $120 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. Taking the walls of the basement to be at \)10^{\circ} \mathrm{C}$ also, determine the rate of heat loss from the hot water. Also, determine the average velocity of the water in the pipe if the temperature of the water drops by \(3^{\circ} \mathrm{C}\) as it passes through the basement.

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