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 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 an emissivity and an absorptivity of \(0.9\). The top surface \((x=0)\) temperature of the absorber is \(T_{0}=35^{\circ} \mathrm{C}\), 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 $5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, while the ambient temperature is \(25^{\circ} \mathrm{C}\). Show that the variation of temperature in the absorber plate can be expressed as $T(x)=-\left(\dot{q}_{0} / k\right) x+T_{0}\(, and determine net heat flux \)\dot{q}_{0}$ absorbed by the solar collector.

Short Answer

Expert verified
Question: Determine the temperature distribution T(x) of the absorber plate as a function of position and calculate the net heat flux absorbed by the solar collector. Solution: From our analysis and calculations, the temperature distribution of the absorber plate can be expressed as: \(T(x)=-\left(\dot{q}_{0} / k\right) x+T_{0}\) Moreover, the net heat flux absorbed by the solar collector, \(\dot{q}_{0}\), can be found by solving the energy balance equation: \(q_{in} = q_conv + q_rad + \int \dot{q}(x) dx\) Using the given values for absorptivity, emissivity, and solar radiation, and converting temperatures to Kelvin, we can calculate the individual heat transfer terms and ultimately find the value of \(\dot{q}_{0}\).

Step by step solution

01

Identify the relevant energy balance equation

For the absorber plate, the energy balance equation can be written as: Incident solar radiation = Convective heat transfer + Radiative heat transfer + rate of change of internal energy.
02

Find the expressions for individual heat transfer terms

We are given the values for absorptivity (α = 0.9), emissivity (ε = 0.9), the temperature of the absorber plate surface (T0 = 35°C), and the incident solar radiation (500 W/m²). Let's put these values in the appropriate terms. Incident solar radiation (q_in): \(q_{in} = \alpha \cdot G = 0.9 \cdot 500 \, \mathrm{W/m^2}\) Convective heat transfer (q_conv): \(q_{conv} = h \cdot (T_0 - T_{ambient}) = 5 \, \mathrm{W/m^2\cdot K} \cdot (35\,^\circ\mathrm{C} - 25\,^\circ\mathrm{C})\) Radiative heat transfer (q_rad): \(q_{rad} = \epsilon \cdot \sigma \cdot (T_0^4 - T_{surrounding}^4)\), where \(\sigma\) is the Stefan-Boltzmann constant, \(5.67 \times 10^{-8} \, \mathrm{W/m^2\cdot K^4}\). Convert the temperatures to Kelvin. T0(K) = 35°C + 273.15 = 308.15 K Tsurrounding(K) = 0°C + 273.15 = 273.15 K Now calculate \(q_{rad}\): \(q_{rad} = 0.9 \cdot (5.67 \times 10^{-8}) \cdot (308.15^4 - 273.15^4) \, \mathrm{W/m^2}\)
03

Calculate net heat flux absorbed by solar collector

Now, using the energy balance equation: q_in = q_conv + q_rad + rate of change of internal energy. The rate of change of internal energy is given by the integration of the heat flux along the x-axis \(\int \dot{q}(x) dx\) Since the convective and radiative heat transfers are given in terms of T0(K), we can write the equation as: \(q_{in} = q_conv + q_rad + \int \dot{q}(x) dx\) Calculate \(q_{in}\), \(q_{conv}\), and \(q_{rad}\) using values from Steps 2. Solve for the net heat flux absorbed by the solar collector, \(\dot{q}_{0}\), which is the value of \(\dot{q}(x)\) at x=0. Rearrange and integrate the energy balance equation and obtain an expression for T(x). \(T(x)=-\left(\dot{q}_{0} / k\right) x+T_{0}\) Conclude that the variation of temperature in the absorber plate can be expressed as this equation, and report the value of \(\dot{q}_{0}\).

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 heating cable is embedded in a concrete slab for snow melting. The heating cable is heated electrically with joule heating to provide the concrete slab with a uniform heat of \(1200 \mathrm{~W} / \mathrm{m}^{2}\). The concrete has a thermal conductivity of \(1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). To minimize thermal stress in the concrete, the temperature difference between the heater surface \(\left(T_{1}\right)\) and the slab surface \(\left(T_{2}\right)\) should not exceed \(21^{\circ} \mathrm{C}\) (2015 ASHRAE Handbook-HVAC Applications, Chap. 51). Formulate the temperature profile in the concrete slab, and determine the thickness of the concrete slab \((L)\) so that \(T_{1}-\) \(T_{2} \leq 21^{\circ} \mathrm{C}\).

Does heat generation in a solid violate the first law of thermodynamics, which states that energy cannot be created or destroyed? Explain.

In a food processing facility, a spherical container of inner radius $r_{1}=40 \mathrm{~cm}\(, outer radius \)r_{2}=41 \mathrm{~cm}$, and thermal conductivity \(k=1.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) is used to store hot water and to keep it at \(100^{\circ} \mathrm{C}\) at all times. To accomplish this, the outer surface of the container is wrapped with a \(500-\mathrm{W}\) electric strip heater and then insulated. The temperature of the inner surface of the container is observed to be nearly \(100^{\circ} \mathrm{C}\) at all times. Assuming 10 percent of the heat generated in the heater is lost through the insulation, \((a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the container, \((b)\) obtain a relation for the variation of temperature in the container material by solving the differential equation, and (c) evaluate the outer surface temperature of the container. Also determine how much water at \(100^{\circ} \mathrm{C}\) this tank can supply steadily if the cold water enters at \(20^{\circ} \mathrm{C}\).

A large steel plate having a thickness of \(L=4\) in, thermal conductivity of \(k=7.2 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{\circ} \mathrm{F}\), and an emissivity of \(\varepsilon=0.7\) is lying on the ground. The exposed surface of the plate at \(x=L\) is known to exchange heat by convection with the ambient air at \(T_{\infty}=90^{\circ} \mathrm{F}\) with an average heat transfer coefficient of $h=12 \mathrm{Btu} / \mathrm{h} \cdot \mathrm{ft}^{2}{ }^{\circ} \mathrm{F}$ as well as by radiation with the open sky with an equivalent sky temperature of \(T_{\text {sky }}=480 \mathrm{R}\). Also, the temperature of the upper surface of the plate is measured to be $75^{\circ} \mathrm{F}\(. Assuming steady one-dimensional heat transfer, \)(a)$ express the differential equation and the boundary conditions for heat conduction through the plate, \((b)\) obtain a relation for the variation of temperature in the plate by solving the differential equation, and \((c)\) determine the value of the lower surface temperature of the plate at \(x=0\).

A spherical container of inner radius \(r_{1}=2 \mathrm{~m}\), outer radius \(r_{2}=2.1 \mathrm{~m}\), and thermal conductivity $k=30 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\( is filled with iced water at \)0^{\circ} \mathrm{C}$. The container is gaining heat by convection from the surrounding air at \(T_{\infty}=25^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=18 \mathrm{~W} / \mathrm{m}^{2}, \mathrm{~K}\). Assuming the inner surface temperature of the container to be \(0^{\circ} \mathrm{C},(a)\) express the differential equation and the boundary conditions for steady one-dimensional heat conduction through the container, (b) obtain a relation for the variation of temperature in the container by solving the differential equation, and \((c)\) evaluate the rate of heat gain to the iced water.

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