Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

A \(0.2-\mathrm{m} \times 0.2-\mathrm{m}\) street sign surface has an absorptivity of \(0.6\) and an emissivity of \(0.7\). Solar radiation is incident on the street sign at a rate of \(200 \mathrm{~W} / \mathrm{m}^{2}\), and the surrounding quiescent air is at \(25^{\circ} \mathrm{C}\). Determine the surface temperature of the street sign. Assume the film temperature is $30^{\circ} \mathrm{C}$.

Short Answer

Expert verified
The surface temperature of the street sign is approximately \(36.15^{\circ} \mathrm{C}\).

Step by step solution

01

Convert the temperature values to Kelvin

Given temperatures are in Celsius, and in heat transfer problems, it's preferable to work in Kelvin. $$T_{surrounding} = 25^{\circ} \mathrm{C} + 273.15 = 298.15 \mathrm{K}$$ $$T_{film} = 30^{\circ} \mathrm{C} + 273.15 = 303.15 \mathrm{K}$$
02

Calculate heat absorbed by the surface due to solar radiation

Given the area of the street sign \(A_s\), absorptivity \(\alpha\), and solar radiation rate \(q_{solar}\), the heat absorbed by the surface due to solar radiation can be calculated as: $$q_{absorbed} = A_s \times \alpha \times q_{solar} = 0.2 \times 0.2 \times 0.6 \times 200 = 4.8\ \mathrm{W}$$
03

Calculate convection heat transfer coefficient

We can use the film temperature for natural convection in quiescent air to find the convection heat transfer coefficient \(h\). A common empirical correlation for the average Nusselt number over a vertical flat plate is given by: $$Nu = 0.15 (Gr \times Pr)^{1/3}$$ Where: Gr is the Grashof number, given by $$Gr = \dfrac{g \beta (T_s - T_{\infty}) L^3}{\nu^2}$$ g is the acceleration due to gravity $$g = 9.81 \mathrm{m/s^2}$$ \(\beta\) is the volume expansion coefficient $$\beta \approx \dfrac{1}{T_f}$$ \(T_s\) is the surface temperature (unknown) \(T_{\infty}\) is the surrounding temperature (298.15 K) \(L\) is the characteristic length, in our case, $$L = 0.2 \mathrm{m}$$ \(\nu\) is the kinematic viscosity of air $$\nu \approx 15.69 \times 10^{-6} \mathrm{m^2/s}$$ at \(T_f = 303.15\ \mathrm{K}\), taken from air properties table Pr is the Prandtl number $$Pr \approx 0.7$$ for air Since we need to solve for the unknown surface temperature \(T_s\), we will use an iterative method. Let's start with an initial surface temperature, say $$T_s = 30^{\circ} \mathrm{C} + 273.15 = 303.15\ \mathrm{K}$$(same as the film temperature) and calculate the Grashof number: $$Gr = \dfrac{9.81 \times \dfrac{1}{303.15} \times (303.15 - 298.15) \times 0.2^3}{(15.69 \times 10^{-6})^2} \approx 3.58 \times 10^5$$ Now, calculate the Nusselt number: $$Nu = 0.15 (3.58 \times 10^5 \times 0.7)^{1/3} \approx 12.31$$ Finally, find the convection heat transfer coefficient: $$h = \dfrac{Nu \times k}{L} \approx \dfrac{12.31 \times 0.02624}{0.2} = 1.60 \mathrm{W/m^2K}$$
04

Set up the heat balance equation

The heat absorbed by the street sign due to solar radiation must be equal to the heat transfer away from the street sign by both radiation and convection: $$q_{absorbed} = q_{radiation} + q_{convection}$$ With known values: $$q_{radiation} = A_s \times \varepsilon \times \sigma (T_s^4 - T_{\infty}^4)$$ $$q_{convection} = A_s \times h (T_s - T_{\infty})$$ Combine the two above equations: $$q_{absorbed} = A_s \times \varepsilon \times \sigma (T_s^4 - T_{\infty}^4) + A_s \times h (T_s - T_{\infty})$$ With given values, $$4.8\ \mathrm{W} = 0.2 \times 0.2 \times 0.7 \times 5.669 \times 10^{-8} (T_s^4 - 298.15^4) + 0.2 \times 0.2 \times 1.60 (T_s - 298.15)$$ Solving for \(T_s\) using an iterative method (or numerical solver) yields: $$T_s \approx 309.3\ \mathrm{K}$$
05

Convert the surface temperature to Celsius

Convert the calculated surface temperature back to Celsius: $$T_s \approx 309.3\ \mathrm{K} - 273.15 = 36.15^{\circ} \mathrm{C}$$ The surface temperature of the street sign is approximately \(36.15^{\circ} \mathrm{C}\).

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

A 0.1-W small cylindrical resistor mounted on a lower part of a vertical circuit board is \(0.3\) in long and has a diameter of \(0.2 \mathrm{in}\). The view of the resistor is largely blocked by another circuit board facing it, and the heat transfer through the connecting wires is negligible. The air is free to flow through the large parallel flow passages between the boards as a result of natural convection currents. If the air temperature near the resistor is \(120^{\circ} \mathrm{F}\), determine the approximate surface temperature of the resistor. Evaluate air properties at a film temperature of \(170^{\circ} \mathrm{F}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption? Answer: \(211^{\circ} \mathrm{F}\)

Consider a vertical plate with length \(L\), placed in quiescent air. If the film temperature is \(20^{\circ} \mathrm{C}\) and the average Nusselt number in natural convection is of the form \(\mathrm{Nu}=\mathrm{CRa}_{L}^{n}\), show that the average heat transfer coefficient can be expressed as $$ \begin{aligned} h &=1.51(\Delta T / L)^{1 / 4} \quad 10^{4}<\mathrm{Ra}_{L}<10^{9} \\ h &=1.19 \Delta T^{1 / 3} \quad 10^{10}<\mathrm{Ra}_{L}<10^{13} \end{aligned} $$

The overall \(U\)-factor of a fixed wood-framed window with double glazing is given by the manufacturer to be $U=2.76 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\( under the conditions of still air inside and winds of \)12 \mathrm{~km} / \mathrm{h}\( outside. What will the \)U$-factor be when the wind velocity outside is doubled? Answer: $2.88 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$

A hot fluid $\left(k_{\text {fluid }}=0.72 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\right)$ is flowing as a laminar fully developed flow inside a pipe with an inner diameter of \(35 \mathrm{~mm}\) and a wall thickness of $5 \mathrm{~mm}\(. The pipe is \)10 \mathrm{~m}$ long, and the outer surface is exposed to air at \(10^{\circ} \mathrm{C}\). The average temperature difference between the hot fluid and the pipe inner surface is $\Delta T_{\text {avg }}=10^{\circ} \mathrm{C}$, and the inner and outer surface temperatures are constant. Determine the outer surface temperature of the pipe. Evaluate the air properties at \(50^{\circ} \mathrm{C}\). Is this a good assumption?

A \(0.5-\mathrm{m}\)-long thin vertical copper plate is subjected to a uniform heat flux of \(1000 \mathrm{~W} / \mathrm{m}^{2}\) on one side, while the other side is exposed to air at \(5^{\circ} \mathrm{C}\). Determine the plate midpoint temperature for \((a)\) a highly polished surface and \((b)\) a black oxidized surface. Hint: The plate midpoint temperature \(\left(T_{L 2}\right)\) has to be found iteratively. Begin the calculations by using a film temperature of \(30^{\circ} \mathrm{C}\).

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free