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Consider a person standing in a room at \(23^{\circ} \mathrm{C}\). Determine the total rate of heat transfer from this person if the exposed surface area and the skin temperature of the person are \(1.7 \mathrm{~m}^{2}\) and $32^{\circ} \mathrm{C}\(, respectively, and the convection heat transfer coefficient is \)5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Take the emissivity of the skin and the clothes to be \(0.9\), and assume the temperature of the inner surfaces of the room to be the same as the air temperature.

Short Answer

Expert verified
Answer: The total rate of heat transfer from the person is 135.83 W.

Step by step solution

01

Convection Heat Transfer Rate

First, we will calculate the convection heat transfer rate using the following formula: \(Q_{conv} = hA(T_{skin} - T_{air})\) Where: \(Q_{conv}\) is the convection heat transfer rate \(h\) is the convection heat transfer coefficient (5 W/m²⋅K) \(A\) is the exposed surface area (1.7 m²) \(T_{skin}\) is the skin temperature (32°C) \(T_{air}\) is the room air temperature (23°C) Plug in the given values: \(Q_{conv} = 5 \mathrm{~W/m}^2\mathrm{~K}\cdot 1.7 \mathrm{~m}^2\cdot (32^{\circ} \mathrm{C} - 23^{\circ} \mathrm{C})\)
02

Calculate Convection Heat Transfer Rate

Calculate \(Q_{conv}\): \(Q_{conv} = 5 \mathrm{~W/m}^2\mathrm{~K}\cdot 1.7 \mathrm{~m}^2 \cdot (9 \mathrm{~K}) = 76.5 \mathrm{~W}\)
03

Radiative Heat Transfer Rate

Now, we will calculate the radiative heat transfer rate using the following formula: \(Q_{rad} = \varepsilon\sigma A (T^4_{skin} - T^4_{air})\) Where: \(Q_{rad}\) is the radiative heat transfer rate \(\varepsilon\) is the emissivity of the skin and clothes (0.9) \(\sigma\) is the Stefan-Boltzmann constant (\(5.67\times10^{-8} \mathrm{~W} / \mathrm{m}^2 \cdot \mathrm{K}^4\)) \(T_{skin}\) and \(T_{air}\) are in Kelvin. First, convert Celsius to Kelvin: \(T_{skin(K)} = 32^{\circ} \mathrm{C}+ 273.15 = 305.15 \mathrm{~K}\) \(T_{air(K)} = 23^{\circ}\mathrm{C}+ 273.15 = 296.15\mathrm{~K}\) Plug in the given values: \(Q_{rad} = 0.9\times 5.67\times10^{-8} \mathrm{~W} / \mathrm{m}^2\mathrm{~K}^4 \cdot 1.7\mathrm{~m}^2 (305.15^4\mathrm{~K}^4 - 296.15^4\mathrm{~K}^4)\)
04

Calculate Radiative Heat Transfer Rate

Calculate \(Q_{rad}\): \(Q_{rad} = 0.9\times 5.67\times 10^{-8}\mathrm{~W} / \mathrm{m}^2\mathrm{~K}^4 \cdot 1.7\mathrm{~m}^2 (8.64\times 10^8\mathrm{~K}^4 - 8.06\times 10^8\mathrm{~K}^4) = 59.33\mathrm{~W}\)
05

Total Heat Transfer Rate

Now, add the convection and radiative heat transfer rates to get the total heat transfer rate: \(Q_{total} = Q_{conv} + Q_{rad}\) Plug in the calculated values: \(Q_{total} = 76.5\mathrm{~W} + 59.33\mathrm{~W} = 135.83\mathrm{~W}\) The total rate of heat transfer from the person is 135.83 W.

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Most popular questions from this chapter

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.

Solve this system of three equations with three unknowns using appropriate software: $$ \begin{aligned} 2 x-y+z &=5 \\ 3 x^{2}+2 y &=z+2 \\ x y+2 z &=8 \end{aligned} $$

An aluminum pan whose thermal conductivity is $237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( has a flat bottom with diameter \)15 \mathrm{~cm}$ and thickness \(0.4 \mathrm{~cm}\). Heat is transferred steadily to boiling water in the pan through its bottom at a rate of \(800 \mathrm{~W}\). If the inner surface of the bottom of the pan is at \(105^{\circ} \mathrm{C}\), determine the temperature of the outer surface of the bottom of the pan.

The rate of heat loss through a unit surface area of a window per unit temperature difference between the indoors and the outdoors is called the \(U\)-factor. The value of the \(U\)-factor ranges from about $1.25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( (or \)0.22 \mathrm{Btw} / \mathrm{h} \cdot \mathrm{ft}^{2} \cdot{ }^{\circ} \mathrm{F}$ ) for low-e coated, argon-filled, quadruple-pane windows to \(6.25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (or $1.1 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$ ) for a single-pane window with aluminum frames. Determine the range for the rate of heat loss through a $1.2-\mathrm{m} \times 1.8-\mathrm{m}\( window of a house that is maintained at \)20^{\circ} \mathrm{C}\( when the outdoor air temperature is \)-8^{\circ} \mathrm{C}$.

A person's head can be approximated as a \(25-\mathrm{cm}\) diameter sphere at \(35^{\circ} \mathrm{C}\) with an emissivity of \(0.95\). Heat is lost from the head to the surrounding air at \(25^{\circ} \mathrm{C}\) by convection with a heat transfer coefficient of $11 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( and by radiation to the surrounding surfaces at \)10^{\circ} \mathrm{C}$. Disregarding the neck, determine the total rate of heat loss from the head. (a) \(22 \mathrm{~W}\) (b) \(27 \mathrm{~W}\) (c) \(49 \mathrm{~W}\) (d) \(172 \mathrm{~W}\) (e) \(249 \mathrm{~W}\)

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