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

Flat-plate solar collectors are often tilted up toward the sun in order to intercept a greater amount of direct solar radiation. The tilt angle from the horizontal also affects the rate of heat loss from the collector. Consider a \(1.5-\mathrm{m}\)-high and 3-m-wide solar collector that is tilted at an angle \(\theta\) from the horizontal. The back side of the absorber is heavily insulated. The absorber plate and the glass cover, which are spaced $2.5 \mathrm{~cm}\( from each other, are maintained at temperatures of \)80^{\circ} \mathrm{C}\( and \)40^{\circ} \mathrm{C}$, respectively. Determine the rate of heat loss from the absorber plate by natural convection for $\theta=0^{\circ}, 30^{\circ}\(, and \)90^{\circ}$.

Short Answer

Expert verified
Answer: The natural convection heat loss from the absorber plate for the given tilt angles are: - For πœƒ = \(0^\circ\): 1080 W - For πœƒ = \(30^\circ\): 1069 W - For πœƒ = \(90^\circ\): negligible

Step by step solution

01

1. List given information and constants

First, let's list the given information for the solar collector: - π‘Žπ‘π‘ π‘œπ‘Ÿπ‘π‘’π‘Ÿ π‘‘π‘’π‘šπ‘π‘’π‘Ÿπ‘Žπ‘‘π‘’π‘Ÿπ‘’ (π‘‡π‘Ž): \(80^{\circ} \mathrm{C}\) - π‘”π‘™π‘Žπ‘ π‘  π‘π‘œπ‘£π‘’π‘Ÿ π‘‘π‘’π‘šπ‘π‘’π‘Ÿπ‘Žπ‘‘π‘’π‘Ÿπ‘’ (𝑇𝑔): \(40^{\circ} \mathrm{C}\) - π‘ π‘œπ‘™π‘Žπ‘Ÿ π‘π‘œπ‘™π‘™π‘’π‘π‘‘π‘œπ‘Ÿ π‘‘π‘–π‘šπ‘’π‘›π‘ π‘–π‘œπ‘›π‘ : \(1.5\, \mathrm{m} \times 3\, \mathrm{m}\) - 𝑑𝑖𝑙𝑑 π‘Žπ‘›π‘”π‘™π‘’(πœƒ): \(0^{\circ},\, 30^{\circ},\, 90^{\circ}\) - π‘Žπ‘π‘ π‘œπ‘Ÿπ‘π‘’π‘Ÿ π‘Žπ‘›π‘‘ π‘”π‘™π‘Žπ‘ π‘  π‘ π‘π‘Žπ‘π‘’: \(2.5\, \mathrm{cm}\) We'll also need the following constants: - Gravitational acceleration (g): \(9.81\, \mathrm{m/s^2}\) - Air kinematic viscosity (Ξ½): \(1.6 \times 10^{-5}\, \mathrm{m^2/s}\) - Air Prandtl number (π‘ƒπ‘Ÿ): 0.7 - Stefan-Boltzmann constant (Οƒ): \(5.67 \times 10^{-8}\, \mathrm{Wm^{-2}K^{-4}}\)
02

2. Calculate the temperature difference and average temperature

We need to find the average temperature (𝑇avg) and the temperature difference (𝑇diff) between the absorber and glass cover to calculate the Grashof number later. 𝑇diff = π‘‡π‘Ž βˆ’ 𝑇𝑔: For the temperatures given, the difference is \(80 - 40 = 40\, ^{\circ}\mathrm{C}\). 𝑇avg = (π‘‡π‘Ž + 𝑇𝑔) / 2: For the temperatures given, the average is \((80 + 40) / 2 = 60\, ^{\circ}\mathrm{C}\).
03

3. Calculate the Grashof number

For each tilt angle, πœƒ, we'll calculate the Grashof number (πΊπ‘Ÿ), which is used to evaluate the natural convection heat transfer coefficient. The Grashof number is given by: \(Gr_\theta = \frac{g\beta L^3 (T_{diff})}{\nu^2}\cos(\theta)\) Where, \(g\) - gravitational acceleration \(\beta\) - coefficient of volume expansion (approximated by π‘π‘’π‘‘π‘Ž = 1 / 𝑇avg for ideal gases) \(L\) - characteristic length (distance between absorber plate and glass cover) \(T_{diff}\) - temperature difference \(\nu\) - air kinematic viscosity \(\theta\) - tilt angle For this problem, the distance \(L\) between the absorber plate and the glass cover is 0.025 m (converted from 2.5 cm), and π‘π‘’π‘‘π‘Ž can be found by \(1 / (273.15 + 60) = 2.414 \times 10^{-3}\, \mathrm{K^{-1}}\). Now, we'll calculate the Grashof number for each tilt angle: \(Gr_0 = \frac{9.81 \times 2.414 \times 10^{-3} \times (0.025)^3 \times 40}{(1.6\times10^{-5})^2} \cos(0^{\circ}) = 1.12 \times 10^5\) \(Gr_{30} = \frac{9.81 \times 2.414 \times 10^{-3} \times (0.025)^3 \times 40}{(1.6\times10^{-5})^2} \cos(30^{\circ}) = 9.72 \times 10^4\) \(Gr_{90} = \frac{9.81 \times 2.414 \times 10^{-3} \times (0.025)^3 \times 40}{(1.6\times10^{-5})^2} \cos(90^{\circ}) = 0 \Rightarrow Gr_{90}<<Gr_{0}, Gr_{30}\)
04

4. Calculate the Nusselt number and heat transfer coefficient

Using the Grashof number calculated in step 3 and the given Prandtl number, π‘ƒπ‘Ÿ, we can find the Nusselt number (𝑁𝑒) using: \(Nu_\theta = C \times (Gr_\theta \cdot Pr)^{1/4}\) We can choose the constant \(C = 0.15\) for a parallel plate configuration in this case. We can then find the heat transfer coefficient (π‘˜) by: \(k_\theta = \frac{Nu_\theta \times k_{air}}{L}\) Where \(k_{air}\) is the air thermal conductivity and is approximately \(k_{air} = 0.0262\, \mathrm{Wm^{-1}K^{-1}}\) at \(60^{\circ}\mathrm{C}\). Now, we can calculate the heat transfer coefficient for each tilt angle: \(k_0 = \frac{(0.15 \times (1.12 \times 10^5 \times 0.7)^{1/4}) \times 0.0262}{0.025} = 6.00\, \mathrm{Wm^{-2}K^{-1}}\) \(k_{30} = \frac{(0.15 \times (9.72 \times 10^4 \times 0.7)^{1/4}) \times 0.0262}{0.025} = 5.94\, \mathrm{Wm^{-2}K^{-1}}\)
05

5. Calculate the heat loss for each tilt angle

Now that we have the heat transfer coefficients for each tilt angle, we can find the heat loss due to natural convection for each case: \(Q_\theta = k_\theta \times A \times T_{diff}\) Where \(A\) is the area of the solar collector. In this case, the area is \(1.5\, \mathrm{m} \times 3\, \mathrm{m} = 4.5\, \mathrm{m^2}\). Finally, we can calculate the heat loss for each tilt angle: \(Q_0 = 6.00 \times 4.5 \times 40 = 1080\, \mathrm{W}\) \(Q_{30} = 5.94 \times 4.5 \times 40 = 1069\, \mathrm{W}\) \(Q_{90}\) is negligible due to the Grashof number being significantly smaller in comparison to \(Gr_0\) and \(Gr_{30}\) The natural convection heat loss from the absorber plate for the given tilt angles are: - For \(\theta = 0^\circ\): \(1080\, \mathrm{W}\) - For \(\theta = 30^\circ\): \(1069\, \mathrm{W}\) - For \(\theta = 90^\circ\): negligible

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 12-cm-diameter and 15-m-long cylinder with a surface temperature of \(10^{\circ} \mathrm{C}\) is placed horizontally in air at $40^{\circ} \mathrm{C}$. Calculate the steady rate of heat transfer for the cases of (a) free-stream air velocity of \(10 \mathrm{~m} / \mathrm{s}\) due to normal winds and (b) no winds and thus a free-stream velocity of zero.

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)$

Consider a house in Atlanta, Georgia, that is maintained at $22^{\circ} \mathrm{C}\( and has a total of \)14 \mathrm{~m}^{2}$ of window area. The windows are double-door-type with wood frames and metal spacers. The glazing consists of two layers of glass with \(12.7\) \(\mathrm{mm}\) of airspace with one of the inner surfaces coated with reflective film. The average winter temperature of Atlanta is \(11.3^{\circ} \mathrm{C}\). Determine the average rate of heat loss through the windows in winter. Answer: \(319 \mathrm{~W}\)

An electronic box that consumes \(200 \mathrm{~W}\) of power is cooled by a fan blowing air into the box enclosure. The dimensions of the electronic box are \(15 \mathrm{~cm} \times 50 \mathrm{~cm} \times 50 \mathrm{~cm}\), and all surfaces of the box are exposed to the ambient environment except the base surface. Temperature measurements indicate that the box is at an average temperature of \(32^{\circ} \mathrm{C}\) when the ambient temperature and the temperature of the surrounding walls are \(25^{\circ} \mathrm{C}\). If the emissivity of the outer surface of the box is \(0.75\), determine the fraction of the heat lost from the outer surfaces of the electronic box.

Consider a heat sink with optimum fin spacing. Explain how heat transfer from this heat sink will be affected by \((a)\) removing some of the fins on the heat sink and (b) doubling the number of fins on the heat sink by reducing the fin spacing. The base area of the heat sink remains unchanged at all times.

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