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A \(0.5-\mathrm{m}\)-long thin vertical plate is subjected to uniform heat flux on one side, while the other side is exposed to cool air at $5^{\circ} \mathrm{C}\(. The plate surface has an emissivity of \)0.73$, and its midpoint temperature is \(55^{\circ} \mathrm{C}\). Determine the heat flux on the plate surface.

Short Answer

Expert verified
Answer: The heat flux on the surface of the thin vertical plate is approximately \(1372.43\,\mathrm{W/m^2}\).

Step by step solution

01

List the given data

The exercise provided us with the following information: Length of the plate, L = \(0.5\,\mathrm{m}\) Midpoint temperature of the plate, T_m = \(55^{\circ}\mathrm{C}\) Temperature of cool air, T_a = \(5^{\circ}\mathrm{C}\) Emissivity of the plate surface, ε = 0.73 First, we need to convert the temperatures to Kelvin: T_m(K) = T_m(C) + 273.15 = \(55 + 273.15 = 328.15\,\mathrm{K}\) T_a(K) = T_a(C) + 273.15 = \(5 + 273.15 = 278.15\,\mathrm{K}\)
02

Calculate the radiated heat flux

The radiated heat flux is given by the Stefan-Boltzmann law for a black body, which states that \(q_{rad} = εσ(T_m^4 - T_a^4)\), where σ is the Stefan-Boltzmann constant (\(5.67\times10^{-8}\,\mathrm{W/m^2K^4}\)). Now we can calculate the radiated heat flux: \(q_{rad} = 0.73\times5.67\times10^{-8}(328.15^4 - 278.15^4) = 1257.16\,\mathrm{W/m^2}\)
03

Calculate the convective heat flux

We will use Newton's Law of cooling to find the convective heat transfer coefficient (h): \(q_{conv} = h(T_m - T_a)\). However, we need to find h first. To do this, we will assume a correlation for the Nusselt number - a dimensionless number, which can be expressed as \(Nu = \frac{hL}{k}\), where L is the characteristic length and k is the thermal conductivity. For vertical surfaces, a rough estimate can be obtained using the correlation: \(Nu = 0.68 + 0.67Ra^{1/4}Pr^{1/3}\), where Ra is the Rayleigh number and Pr is the Prandtl number. The Rayleigh number is given by \(Ra = Gr \times Pr\), where Gr is the Grashof number. The Prandtl number is a material property and for air at room temperature is approximately 0.7. The Grashof number is given by: \(Gr = \frac{g\beta(T_m - T_a)L^3}{\nu^2}\), where g is the acceleration due to gravity (\(9.81\,\mathrm{m/s^2}\)), β is the coefficient of thermal expansion of air (approximately \(3.56\times10^{-3}\,\mathrm{K^{-1}}\)) and ν is the kinematic viscosity of air (approximately \(15.7\times10^{-6}\,\mathrm{m^2/s}\)). Now, we can calculate Gr: \(Gr = \frac{9.81\times3.56\times10^{-3}(328.15-278.15)(0.5)^3}{(15.7\times10^{-6})^2} = 2.595\times10^8\) Next, we can find Ra: \(Ra = Gr\times Pr = 2.595\times10^8\times0.7 = 1.817\times10^8\). Now we can calculate Nu: \(Nu = 0.68 + 0.67(1.817\times10^8)^{1/4}(0.7)^{1/3} = 44.11\) Finally, we can determine the heat transfer coefficient h: \(h = \frac{Nu\times k}{L} = \frac{44.11\times 0.026}{0.5} = 2.31\,\mathrm{W/m^2K}\) Now, using Newton's Law of Cooling, we can find the convective heat flux, \(q_{conv}\): \(q_{conv} = h(T_m - T_a) = 2.31(328.15 - 278.15) = 115.27\,\mathrm{W/m^2}\)
04

Determine the total heat flux

The total heat flux on the plate surface is the sum of the radiated and convective heat fluxes: \(q_{total} = q_{rad} + q_{conv} = 1257.16 + 115.27 = 1372.43\,\mathrm{W/m^2}\) The heat flux on the plate surface is approximately \(1372.43\,\mathrm{W/m^2}\).

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Most popular questions from this chapter

A vertical \(0.9\)-m-high and \(1.5\)-m-wide double-pane window consists of two sheets of glass separated by a \(2.0-\mathrm{cm}\) air gap at atmospheric pressure. If the glass surface temperatures across the air gap are measured to be \(20^{\circ} \mathrm{C}\) and \(30^{\circ} \mathrm{C}\), the rate of heat transfer through the window is (a) \(16.3 \mathrm{~W}\) (b) \(21.7 \mathrm{~W}\) (c) \(24.0 \mathrm{~W}\) $\begin{array}{ll}\text { (d) } 31.3 \mathrm{~W} & \text { (e) } 44.6 \mathrm{~W}\end{array}$ (For air, use $k=0.02551 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \quad \operatorname{Pr}=0.7296\(, \)\nu=1.562 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\(. Also, the applicable correlation is \)\left.\mathrm{Nu}=0.42 \mathrm{Ra}^{1 / 4} \operatorname{Pr}^{0.012}(H / L)^{-0.3} .\right)$

In an ordinary double-pane window, about half of the heat transfer is by radiation. Describe a practical way of reducing the radiation component of heat transfer.

A can of engine oil with a length of \(150 \mathrm{~mm}\) and a diameter of $100 \mathrm{~mm}$ is placed vertically in the trunk of a car. On a hot summer day, the temperature in the trunk is \(43^{\circ} \mathrm{C}\). If the surface temperature of the can is \(17^{\circ} \mathrm{C}\), determine heat transfer rate from the can surface. Neglect the heat transfer from the ends of the can.

Skylights or "roof windows" are commonly used in homes and manufacturing facilities since they let natural light in during daytime and thus reduce the lighting costs. However, they offer little resistance to heat transfer, and large amounts of energy are lost through them in winter unless they are equipped with a motorized insulating cover that can be used in cold weather and at nights to reduce heat losses. Consider a \(1-\mathrm{m}\)-wide and \(2.5\)-m-long horizontal skylight on the roof of a house that is kept at \(20^{\circ} \mathrm{C}\). The glazing of the skylight is made of a single layer of \(0.5-\mathrm{cm}\)-thick glass $(k=0.78 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( and \)\varepsilon=0.9$ ). Determine the rate of heat loss through the skylight when the air temperature outside is \(-10^{\circ} \mathrm{C}\) and the effective sky temperature is \(-30^{\circ} \mathrm{C}\). Compare your result with the rate of heat loss through an equivalent surface area of the roof that has a common \(R-5.34\) construction in SI units (i.e., a thickness-to- effective-thermal-conductivity ratio of $5.34 \mathrm{~m}^{2} . \mathrm{K} / \mathrm{W}\( ). Evaluate air properties at a film temperature of \)-7^{\circ} \mathrm{C}\( and \)1 \mathrm{~atm}$ pressure. Is this a good assumption?

Consider a cylinder with a length of \(15 \mathrm{~cm}\) and a diameter of $10 \mathrm{~cm}\(. The cylinder has a surface temperature of \)43^{\circ} \mathrm{C}\(, while the room air temperature is \)17^{\circ} \mathrm{C}$. Determine whether placing the cylinder horizontally or vertically would achieve a higher heat transfer rate.

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