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A 1000-W iron is left on an ironing board with its base exposed to the air at \(20^{\circ} \mathrm{C}\). The convection heat transfer coefficient between the base surface and the surrounding air is $35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\(. If the base has an emissivity of \)0.6$ and a surface area of \(0.02 \mathrm{~m}^{2}\), determine the temperature of the base of the iron. Answer: \(674^{\circ} \mathrm{C}\)

Short Answer

Expert verified
Answer: The temperature of the base of the iron is approximately 674°C.

Step by step solution

01

Determine the total heat transfer equation

Since the iron is exposed to the air, the heat transfer will occur by both convection and radiation. We need to find the total heat transfer, which is given by the sum of heat transfer due to convection and radiation: $$ q_{total} = q_{conv} + q_{rad} $$
02

Set up the convection heat transfer equation

The convection heat transfer is given by the following formula: $$ q_{conv} = hA(T_{base} - T_{air}) $$ where h is the convection heat transfer coefficient, A is the base surface area, \(T_{base}\) is the base temperature, and \(T_{air}\) is the air temperature.
03

Set up the radiation heat transfer equation

The radiation heat transfer is given by the following formula: $$ q_{rad} = \epsilon \sigma A(T_{base}^4 - T_{air}^4) $$ where \(\epsilon\) is the emissivity, \(\sigma\) is the Stefan-Boltzmann constant (\(5.67 \times 10^{-8} \mathrm{W} / \mathrm{m}^2 \cdot \mathrm{K}^4\)), and all other variables are as defined previously.
04

Set up the total heat transfer equation

We know that the iron has a power of 1000 W. The total heat transfer is equal to the power of the iron, so substituting the convection and radiation equations into the total heat transfer equation, we get: $$ 1000 = hA(T_{base} - T_{air}) + \epsilon \sigma A(T_{base}^4 - T_{air}^4) $$
05

Substitute given values

Now, we can substitute the given values into the equation: $$ 1000 = 35 (0.02) (T_{base} - 20) + 0.6 (5.67 \times 10^{-8}) (0.02)(T_{base}^4 - 20^4) $$ This equation is a nonlinear equation in terms of \(T_{base}\). To solve for \(T_{base}\), we will use an iterative numerical method.
06

Solve the nonlinear equation

We can use the Newton-Raphson method, or a root-finding method like the bisection method, or a solver software to find the root of the function. Solving the given equation using any of these methods, we find the value of \(T_{base}\): $$ T_{base} \approx 947 \mathrm{K} $$ Note that the answer is in Kelvin.
07

Convert the temperature to Celsius

To convert the temperature from Kelvin to Celsius, use the following formula: $$ T_{\mathrm{C}} = T_{\mathrm{K}} - 273.15 $$ Substituting the obtained temperature in Kelvin, we get: $$ T_{\mathrm{C}} \approx 947 - 273.15 = 673.85^{\circ} \mathrm{C} $$ Rounding the answer to the nearest whole number, we find that the temperature of the base of the iron is approximately \(674^{\circ} \mathrm{C}\).

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Most popular questions from this chapter

Consider a person whose exposed surface area is \(1.7 \mathrm{~m}^{2}\), emissivity is \(0.5\), and surface temperature is \(32^{\circ} \mathrm{C}\). Determine the rate of heat loss from that person by radiation in a large room having walls at a temperature of (a) \(300 \mathrm{~K}\) and (b) $280 \mathrm{~K}$.

A flat-plate solar collector is used to heat water by having water flow through tubes attached at the back of the thin solar absorber plate. The absorber plate has a surface area of \(2 \mathrm{~m}^{2}\) with emissivity and absorptivity of \(0.9\). The surface temperature of the absorber is $35^{\circ} \mathrm{C}\(, and solar radiation is incident on the absorber at \)500 \mathrm{~W} / \mathrm{m}^{2}\( with a surrounding temperature of \)0^{\circ} \mathrm{C}$. The convection heat transfer coefficient at the absorber surface is \(5 \mathrm{~W} / \mathrm{m}^{2}\). \(\mathrm{K}\), while the ambient temperature is \(25^{\circ} \mathrm{C}\). Net heat absorbed by the solar collector heats the water from an inlet temperature $\left(T_{\text {in }}\right)\( to an outlet temperature \)\left(T_{\text {out }}\right)$. If the water flow rate is \(5 \mathrm{~g} / \mathrm{s}\) with a specific heat of $4.2 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}$, determine the temperature rise of the water.

An engineer who is working on the heat transfer analysis of a house in English units needs the convection heat transfer coefficient on the outer surface of the house. But the only value he can find from his handbooks is $14 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, which is in SI units. The engineer does not have a direct conversion factor between the two unit systems for the convection heat transfer coefficient. Using the conversion factors between \(\mathrm{W}\) and \(\mathrm{Btu} / \mathrm{h}, \mathrm{m}\) and \(\mathrm{ft}\), and \({ }^{\circ} \mathrm{C}\) and \({ }^{\circ} \mathrm{F}\), express the given convection heat transfer coefficient in Btu/h \(\mathrm{ft}^{2}{ }^{\circ} \mathrm{F}\). Answer: \(2.47\) Btu/h $\cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$

A 2-in-diameter spherical ball whose surface is maintained at a temperature of \(170^{\circ} \mathrm{F}\) is suspended in the middle of a room at $70^{\circ} \mathrm{F}\(. If the convection heat transfer coefficient is \)15 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}{ }^{2}{ }^{\circ} \mathrm{F}$ and the emissivity of the surface is \(0.8\), determine the total rate of heat transfer from the ball.

Steady heat conduction occurs through a \(0.3\)-m-thick, $9-\mathrm{m} \times 3-\mathrm{m}\( composite wall at a rate of \)1.2 \mathrm{~kW}$. If the inner and outer surface temperatures of the wall are \(15^{\circ} \mathrm{C}\) and \(7^{\circ} \mathrm{C}\), the effective thermal conductivity of the wall is $\begin{array}{ll}\text { (a) } 0.61 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K} & \text { (b) } 0.83 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\end{array}$ (c) \(1.7 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (d) \(2.2 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) (e) \(5.1 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\)

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