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An electric resistance space heater is designed such that it resembles a rectangular box \(50 \mathrm{~cm}\) high, \(80 \mathrm{~cm}\) long, and $15 \mathrm{~cm}\( wide filled with \)45 \mathrm{~kg}$ of oil. The heater is to be placed against a wall, and thus heat transfer from its back surface is negligible. The surface temperature of the heater is not to exceed $75^{\circ} \mathrm{C}\( in a room at \)25^{\circ} \mathrm{C}$ for safety considerations. Disregarding heat transfer from the bottom and top surfaces of the heater in anticipation that the top surface will be used as a shelf, determine the power rating of the heater in W. Take the emissivity of the outer surface of the heater to be \(0.8\) and the average temperature of the ceiling and wall surfaces to be the same as the room air temperature. Also, determine how long it will take for the heater to reach steady operation when it is first turned on (i.e., for the oil temperature to rise from \(25^{\circ} \mathrm{C}\) to \(75^{\circ} \mathrm{C}\) ). State your assumptions in the calculations.

Short Answer

Expert verified
Step 1: Calculate the surface area of the heater. A = (0.50 m) x (0.80 m) = 0.4 m² Step 2: Calculate the power rating using the Stefan-Boltzmann Law. q = εσA(Ts^4 - Tr^4) = 0.8 × 5.67 × 10^(-8) × 0.4 × (348^4 - 298^4) ≈ 427.5 W Step 3: Calculate the energy required to raise the oil temperature. E = mcΔT = 45 kg × 2.0 × 10^3 J/kg.K × 50 K = 4.5 × 10^6 J Step 4: Calculate the time taken to reach steady-state operation. t = E/q = (4.5 × 10^6 J) / (427.5 W) ≈ 10526.4 s, which is approximately 175.4 minutes. Answer: The power rating of the space heater is 427.5 W, and it takes approximately 175.4 minutes to reach steady-state operation.

Step by step solution

01

Calculate the surface area of the heater

Since heat transfer from the back, bottom, and top surface is negligible, we only need the surface area of the front surface. The front surface has dimensions \(50 \mathrm{~cm}\) in height and \(80 \mathrm{~cm}\) in length. Convert these dimensions to meters and multiply them to get the surface area: \[ A = (0.50 \,\text{m})\times(0.80\, \text{m}) \]
02

Calculate the power rating using the Stefan-Boltzmann Law

The Stefan-Boltzmann law states that the heat transfer rate through radiation can be calculated as follows: \[ q = \epsilon \sigma A(T_s^4 - T_r^4) \] Here, \(\epsilon = 0.8\) is the emissivity, \(\sigma = 5.67\times10^{-8} \,\text{W/m}^2\text{K}^4\) is the Stefan-Boltzmann constant, \(T_s = 75^{\circ}\text{C} = 348\,\text{K}\) is the surface temperature, and \(T_r = 25^{\circ}\text{C} = 298\,\text{K}\) is the room air temperature. Plug in all the values and solve for the heat transfer rate \(q\), which is equal to the power rating of the heater.
03

Calculate the energy required to raise the oil temperature

To determine the energy required to raise the oil temperature from \(25^{\circ}\text{C}\) to \(75^{\circ}\text{C}\), we use the following equation: \[ E = mc\Delta T \] where \(m = 45\,\text{kg}\) is the mass of oil, and \(c\) is the specific heat capacity of the oil. Assuming the oil is similar to a common mineral oil, the specific heat capacity is approximately \(c = 2.0 \times 10^3 \,\text{J/kg}\cdot\text{K}\). Calculate the energy \(E\) using the given values and the temperature difference \(\Delta T = 50\,\text{K}\).
04

Calculate the time taken to reach steady-state operation

Since the power rating of the heater (the heat transfer rate) is known, we can calculate the time taken to reach steady-state operation: \[ t = \frac{E}{q} \] where \(t\) is the time taken in seconds. Substitute the calculated energy \(E\) and power rating \(q\) to obtain the time taken to reach steady-state operation. You may want to convert the result to minutes for convenience.

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Most popular questions from this chapter

A vertical \(1.5-\mathrm{m}\)-high and \(3.0\)-m-wide enclosure consists of two surfaces separated by a \(0.4-\mathrm{m}\) air gap at atmospheric pressure. If the surface temperatures across the air gap are measured to be $280 \mathrm{~K}\( and \)336 \mathrm{~K}\( and the surface emissivities to be \)0.15$ and \(0.90\), determine the fraction of heat transferred through the enclosure by radiation. Arswer: \(0.30\)

Consider an ordinary house with \(R-13\) walls (walls that have an \(R\)-value of $\left.13 \mathrm{~h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F} / \mathrm{B} t \mathrm{u}\right)\(. Compare this to the \)R$-value of the common double-door windows that are double pane with \(\frac{1}{4}\) in of airspace and have aluminum frames. If the windows occupy only 20 percent of the wall area, determine if more heat is lost through the windows or through the remaining 80 percent of the wall area. Disregard infiltration losses.

The side surfaces of a 3 -m-high cubic industrial furnace burning natural gas are not insulated, and the temperature at the outer surface of this section is measured to be \(110^{\circ} \mathrm{C}\). The temperature of the furnace room, including its surfaces, is \(30^{\circ} \mathrm{C}\), and the emissivity of the outer surface of the furnace is \(0.7\). It is proposed that this section of the furnace wall be insulated with glass wool insulation $(k=0.038 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$ wrapped by a reflective sheet \((\varepsilon=0.2)\) in order to reduce the heat loss by 90 percent. Assuming the outer surface temperature of the metal section still remains at about \(110^{\circ} \mathrm{C}\), determine the thickness of the insulation that needs to be used. The furnace operates continuously throughout the year and has an efficiency of 78 percent. The price of the natural gas is \(\$ 1.10 /\) therm ( 1 therm \(=105,500 \mathrm{~kJ}\) of energy content). If the installation of the insulation will cost \(\$ 550\) for materials and labor, determine how long it will take for the insulation to pay for itself from the energy it saves.

A 4 -m-long section of a 5-cm-diameter horizontal pipe in which a refrigerant flows passes through a room at \(20^{\circ} \mathrm{C}\). The pipe is not well insulated, and the outer surface temperature of the pipe is observed to be \(-10^{\circ} \mathrm{C}\). The emissivity of the pipe surface is \(0.85\), and the surrounding surfaces are at \(15^{\circ} \mathrm{C}\). The fraction of heat transferred to the pipe by radiation is (a) \(0.24\) (b) \(0.30\) (c) \(0.37\) (d) \(0.48\) (e) \(0.58\) (For air, use $k=0.02401 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \mathrm{Pr}=0.735$, $$ \left.\nu=1.382 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right) $$

A vertical double-pane window consists of two sheets of glass separated by a \(1.2-\mathrm{cm}\) air gap at atmospheric pressure. The glass surface temperatures across the air gap are measured to be \(278 \mathrm{~K}\) and $288 \mathrm{~K}$. If it is estimated that the heat transfer by convection through the enclosure is \(1.5\) times that by pure conduction and that the rate of heat transfer by radiation through the enclosure is about the same magnitude as the convection, the effective emissivity of the two glass surfaces is (a) \(0.35\) (b) \(0.48\) (c) \(0.59\) (d) \(0.84\) (e) \(0.72\)

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