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In a solar pond, the absorption of solar energy can be modeled as heat generation and can be approximated by $\dot{e}_{\text {gen }}=\dot{e}_{0} \dot{e}^{-b x}\(, where \)\dot{e}_{0}$ is the rate of heat absorption at the top surface per unit volume and \(b\) is a constant. Obtain a relation for the total rate of heat generation in a water layer of surface area \(A\) and thickness \(L\) at the top of the pond.

Short Answer

Expert verified
Answer: The relation for the total rate of heat generation in a water layer of surface area A and thickness L at the top of the pond is given by the formula \(E_\text{total} = A\left(\frac{\dot{e}_{0}}{b}\right) \left(1 - \mathrm{e}^{-b L}\right)\).

Step by step solution

01

Understand the heat absorption equation

The equation \(\dot{e}_{\text {gen }}=\dot{e}_{0}\dot{e}^{-b x}\) represents the instantaneous heat generation per unit volume at a distance x from the top surface of the layer. \(\dot{e}_{0}\) is the initial rate of heat absorption at x = 0 (top surface) and b is a constant.
02

Integrate the equation to find the total heat generation

In order to find the total heat generation in the layer of thickness L, we will integrate the equation with respect to the thickness x from 0 to L: $$ E_\text{gen} = \int_0^L \dot{e}_{\text {gen }} dx = \int_0^L \dot{e}_{0} \cdot \mathrm{e}^{-b x} dx $$
03

Evaluate the integral

Now we will evaluate the integral using integration by substitution: $$ \begin{aligned} E_\text{gen} &= \frac{\dot{e}_{0}}{-b} \cdot \mathrm{e}^{-b x} \Big |_{0}^{L} \\ &= \frac{\dot{e}_{0}}{-b} \left[\mathrm{e}^{-b L} - \mathrm{e}^{0}\right] \\ &= \frac{\dot{e}_{0}}{b} \left(1 - \mathrm{e}^{-b L}\right) \end{aligned} $$ At this point, we have found the total heat generation per unit volume of the water layer with thickness L.
04

Relate the result to the surface area A

In order to find the total rate of heat generation in a water layer of surface area A, we need to multiply the total heat generation per unit volume (derived in Step 3) by the surface area A: $$ E_\text{total} = A \cdot E_\text{gen} = A\left(\frac{\dot{e}_{0}}{b}\right) \left(1 - \mathrm{e}^{-b L}\right) $$
05

Final result

The relation for the total rate of heat generation in a water layer of surface area A and thickness L at the top of the pond is: $$ E_\text{total} = A\left(\frac{\dot{e}_{0}}{b}\right) \left(1 - \mathrm{e}^{-b L}\right) $$

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Most popular questions from this chapter

The temperatures at the inner and outer surfaces of a \(15-\mathrm{cm}\)-thick plane wall are measured to be \(40^{\circ} \mathrm{C}\) and $28^{\circ} \mathrm{C}$, respectively. The expression for steady, one-dimensional variation of temperature in the wall is (a) \(T(x)=28 x+40\) (b) \(T(x)=-40 x+28\) (c) \(T(x)=40 x+28\) (d) \(T(x)=-80 x+40\) (e) \(T(x)=40 x-80\)

A circular metal pipe has a wall thickness of \(10 \mathrm{~mm}\) and an inner diameter of \(10 \mathrm{~cm}\). The pipe's outer surface is subjected to a uniform heat flux of \(5 \mathrm{~kW} / \mathrm{m}^{2}\) and has a temperature of \(500^{\circ} \mathrm{C}\). The metal pipe has a variable thermal conductivity given as \(k(T)=k_{0}(1+\beta T)\), where $k_{0}=7.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\beta=0.0012 \mathrm{~K}^{-1}\(, and \)T$ is in \(\mathrm{K}\). Determine the inner surface temperature of the pipe.

Consider steady one-dimensional heat conduction through a plane wall, a cylindrical shell, and a spherical shell of uniform thickness with constant thermophysical properties and no thermal energy generation. The geometry in which the variation of temperature in the direction of heat transfer will be linear is (a) plane wall (b) cylindrical shell (c) spherical shell (d) all of them (e) none of them

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A solar heat flux \(\dot{q}_{s}\) is incident on a sidewalk whose thermal conductivity is \(k\), solar absorptivity is \(\alpha_{s^{+}}\)and convective heat transfer coefficient is \(h\). Taking the positive \(x\)-direction to be toward the sky and disregarding radiation exchange with the surrounding surfaces, the correct boundary condition for this sidewalk surface is (a) \(-k \frac{d T}{d x}=\alpha_{s} \dot{q}_{s}\) (b) \(-k \frac{d T}{d x}=h\left(T-T_{\infty}\right)\) (c) \(-k \frac{d T}{d x}=h\left(T-T_{o c}\right)-\alpha_{s} \dot{q}_{s}\) (d) \(h\left(T-T_{\infty}\right)=\alpha_{s} \dot{q}_{s}\) (e) None of them

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