/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 46 A solar pond operates on the pri... [FREE SOLUTION] | 91Ó°ÊÓ

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A solar pond operates on the principle that heat losses from a shallow layer of water, which acts as a solar absorber, may be minimized by establishing a stable vertical salinity gradient in the water. In practice such a condition may be achieved by applying a layer of pure salt to the bottom and adding an overlying layer of pure water. The salt enters into solution at the bottom and is transferred through the water layer by diffusion, thereby establishing salt-stratified conditions. As a first approximation, the total mass density \(\rho\) and the diffusion coefficient for salt in water \(\left(D_{\mathrm{AB}}\right)\) may be assumed to be constant, with \(D_{\mathrm{AB}}=1.2 \times 10^{-9} \mathrm{~m}^{2} / \mathrm{s}\). (a) If a saturated density of \(\rho_{\mathrm{A}, s}\) is maintained for salt in solution at the bottom of the water layer of thickness \(L=1 \mathrm{~m}\), how long will it take for the mass density of salt at the top of the layer to reach \(25 \%\) of saturation? (b) In the time required to achieve \(25 \%\) of saturation at the top of the layer, how much salt is transferred from the bottom into the water per unit surface area \(\left(\mathrm{kg} / \mathrm{m}^{2}\right)\) ? The saturation density of salt in solution is \(\rho_{A, s}=380 \mathrm{~kg} / \mathrm{m}^{3}\). (c) If the bottom is depleted of salt at the time that the salt density reaches \(25 \%\) of saturation at the top, what is the final (steady-state) density of the salt at the bottom? What is the final density of the salt at the top?

Short Answer

Expert verified
To solve this problem, we first set up a 1-dimensional diffusion model governed by Fick's Second Law, using the given diffusion coefficient for salt in water. We then solve the partial differential equation for the salt concentration \(C_A(x,t)\) as a function of position and time using separation of variables with boundary and initial conditions. This allows us to find the time it takes for the mass density of salt at the top of the layer to reach \(25\%\) of saturation. Next, we calculate the total amount of salt transferred from the bottom into the water per unit surface area by integrating the diffusion flux \(J_A\) over the thickness of the water layer and the time it takes for the salinity to reach \(25\%\) at the top of the layer. Finally, we find the final steady-state density of the salt as a function of position by setting the time derivative of \(C_A(x,t)\) to zero and solving the resulting equation. Evaluating this function at the bottom (x = 0) and at the top (x = L) of the water layer provides the final steady-state density of the salt at the top and bottom, respectively.

Step by step solution

01

Understand the problem and parameters

First, let's understand the given data. We are given: - Diffusion coefficient for salt in water \(D_{AB} = 1.2\times 10^{-9}\,\mathrm{m}^2/\mathrm{s}\) - Water layer thickness \(L = 1\,\mathrm{m}\) - Saturated density of salt in solution \(\rho_{A,s} = 380\,\mathrm{kg}/\mathrm{m}^3\) Now, let's understand the problem. We need to find: (a) Time to reach \(25\%\) saturation at the top of the water layer (b) Amount of salt transferred per unit surface area (c) Final steady-state density of salt at the top and bottom of the water layer.
02

Use the Diffusion Equation

We know that diffusion is governed by Fick's Second Law, which states that the diffusion flux \(J_A\) is proportional to the gradient of the solute concentration \(C_A\) in solution: \[J_A = -D_{AB}\frac{dC_A}{dx}\] Here, \(x\) is the spatial direction along which diffusion is occurring, and \(D_{AB}\) is the diffusion coefficient for salt in water. Assuming a simple 1-dimensional diffusion model and uniform diffusivity throughout the layer, we can write Fick's Second Law as: \[\frac{\partial C_A}{\partial t} = D_{AB}\frac{\partial^2 C_A}{\partial x^2}\] With the initial conditions and boundary conditions (i.e., \(C_A(x,0)\) and \(C_A(0,t)\)), we can solve for \(C_A(x,t)\) as a function of position and time.
03

Apply the given data to the Diffusion Equation

From the initial conditions, we can write: - At \(t=0\), \(C_A(x,0) = 0\) for \(0 < x < L\) and \(C_A(0,0) = \rho_{A,s}\) - At \(0 < t\), \(C_A(0,t) = \rho_{A,s}\) (constant bottom salinity) The goal is to find the time \(t\) when \(C_A(L,t) = 0.25\rho_{A,s}\). The given diffusion coefficient \(D_{AB}\) can be substituted into the diffusion equation to find \(C_A(x,t)\). To solve the diffusion equation with the given boundary and initial conditions, we can employ the method of separation of variables. This involves assuming the following functional form for \(C_A(x,t)\): \[C_A(x,t) = X(x)T(t)\] Substituting this into the diffusion equation, and solving for the temporal and spatial components, will result in an eigenvalue problem for the spatial component \(X(x)\). The eigenfunctions will form a basis for the solution to the diffusion equation, and the coefficients of the eigenfunctions can be determined by applying the initial condition for \(C_A(x,0)\).
04

Determine the time when salinity reaches 25% saturation

We can use the computed function \(C_A(x,t)\) to find the time \(t\) when \(C_A(L,t) = 0.25\rho_{A,s}\). Solving the equation: \[C_A(L,t) = 0.25\rho_{A,s}\] This will give us the time it takes for the mass density of salt at the top of the layer to reach \(25\%\) of saturation.
05

Calculate the amount of salt transferred

To find the amount of salt transferred from the bottom into the water per unit surface area, we can integrate the diffusion flux \(J_A\) over the thickness of the water layer from \(0\) to \(L\) and from \(0\) to the time \(t\): \[\int_0^L \int_0^t J_A(x,\tau) d\tau dx\] With the diffusion flux defined as \(J_A=-D_{AB}\frac{dC_A}{dx}\), substituting this into the integral and evaluating it will give the amount of salt transferred from the bottom into the water per unit surface area in the time it takes for the salinity to reach \(25\%\) at the top of the layer.
06

Determine the final steady-state density

To find the final (steady-state) density of the salt at the bottom and the top of the water layer, we can take the time derivative of \(C_A(x,t)\) and set it to zero. This equation represents the steady-state condition: \[\frac{\partial C_A(x,t)}{\partial t} = 0\] Solving this equation for \(C_A(x)\) will give us the final steady-state density as a function of position. Then, by evaluating this function at \(x=0\) (the bottom) and \(x=L\) (the top), we will obtain the final steady-state density of the salt at the bottom and the top of the water layer, respectively.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Diffusion Coefficient
The diffusion coefficient, often symbolized as \( D \), is a crucial element in understanding how substances spread over time through liquids, gases, or solids. In this specific scenario, we're examining the diffusion of salt in water, with a given diffusion coefficient \( D_{\text{AB}} = 1.2 \times 10^{-9} \; \text{m}^2/\text{s} \).
This value tells us how quickly salt molecules move from the high concentration region at the bottom to the lower concentration region towards the top.
Liquids generally have lower diffusion coefficients compared to gases because liquid molecules are more densely packed, making it more challenging for them to move around.
  • The diffusion coefficient is extremely important in predicting how long it'll take for the salt to reach a certain concentration level at the top.
  • It's dependent on factors such as temperature, size of the molecules, and the properties of both the solute and the solvent.
Salinity Gradient
In a solar pond, a crucial aspect is the establishment of a salinity gradient. This gradient involves a shift from higher salinity (more concentrated salt solution) at the bottom to lower salinity at the top. By stacking layers of different salt concentrations, the advancement of salt toward the surface layer is by diffusion.
Creating this gradient is beneficial for the pond's functionality because:
  • It helps maintain heat by limiting convection, thereby acting like an insulator.
  • The stability of the salinity gradient prevents significant mixing of water layers, which is key to minimizing heat loss.
This gradient is crucial in preventing heat, absorbed by solar radiation at the pond's bottom, from escaping to the air readily. As the diffusion progresses, maintaining a gradient ensures the sustainability and efficiency of a solar pond.
Fick's Second Law
Fick's Second Law of Diffusion is at the heart of how the distribution of salt changes over time in a body of water. This law is expressed by the equation:
\[\frac{\partial C_A}{\partial t} = D_{\text{AB}} \frac{\partial^2 C_A}{\partial x^2}\]
Here, \( C_A \) represents the concentration of salt, \( t \) is time, and \( x \) is the position within the water layer.
This law reveals that the change in concentration over time depends on the spatial change in concentration. It explains why and how salt concentration at any point will approach equilibrium as time progresses.
  • The law helps in determining the rate at which salt spreads within the water.
  • Fick's law is crucial when calculating required time for salt concentration at various points, such as the surface, to reach a particular level.
In practice, solving Fick's Second Law allows us to predict how long diffusion will take under set conditions, like those in a solar pond.
Solar Pond
A solar pond is an innovative energy device that utilizes a salinity gradient to capture and store solar energy. The mechanics behind it involve a thick layer of salt water at the bottom and a less concentrated upper layer. This type of energy system can be extremely efficient in sunny regions.
  • The bottom layer, enriched with salt, acts as a thermal trap, collecting heat from solar radiation.
  • The design utilizes the natural gradient to inhibit convection currents that would otherwise disperse the trapped heat.
By maintaining the salinity gradient, these ponds are capable of storing solar energy for extended periods. This makes solar ponds a sustainable and low-cost renewable energy solution. They can be used for heating, power generation, and desalination, among other applications, due to their ability to consistently maintain and utilize captured heat.
Mass Density
Mass density, often denoted as \( \rho \), is a fundamental property describing the mass of a substance contained within a unit volume. In the context of the solar pond problem exercise, the mass density of salt in solution is particularly relevant.
  • The density of the saturated salt solution at the bottom is given as \( 380 \, \text{kg/m}^3 \); it informs us how heavy and compact the salt solution is.
  • As the salt diffuses up through the water column, its mass density changes proportionally.
Understanding mass density is vital, as differences in density between layers of water can help establish or maintain stability in systems like solar ponds. It serves as a guide to predict how concentrations of materials like salt distribute over time, especially when influenced by diffusion and gravity.

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Most popular questions from this chapter

An open pan of diameter \(0.2 \mathrm{~m}\) and height \(80 \mathrm{~mm}\) (above water at \(27^{\circ} \mathrm{C}\) ) is exposed to ambient air at \(27^{\circ} \mathrm{C}\) and \(25 \%\) relative humidity. Determine the evaporation rate, assuming that only mass diffusion occurs. Determine the evaporation rate, considering bulk motion.

A person applies an insect repellent onto an exposed area of \(A=0.5 \mathrm{~m}^{2}\) of their body. The mass of spray used is \(M=10\) grams, and the spray contains \(25 \%\) (by mass) active ingredient. The inactive ingredient quickly evaporates from the skin surface. (a) If the spray is applied uniformly and the density of the dried active ingredient is \(\rho=2000 \mathrm{~kg} / \mathrm{m}^{3}\), determine the initial thickness of the film of active ingredient on the skin surface. The temperature, molecular weight, and saturation pressure of the active ingredient are \(32^{\circ} \mathrm{C}, 152 \mathrm{~kg} / \mathrm{kmol}\), and \(1.2 \times 10^{-5}\) bars, respectively. (b) If the convection mass transfer coefficient associated with sublimation of the active ingredient to the air is \(\bar{h}_{m}=5 \times 10^{-3} \mathrm{~m} / \mathrm{s}\), the partition coefficient associated with the ingredient-skin interface is \(K=0.05\), and the mass diffusivity of the active ingredient in the skin is \(D_{\mathrm{AB}}=1 \times 10^{-13} \mathrm{~m}^{2} / \mathrm{s}\), determine how long the insect repellent remains effective. The partition coefficient is the ratio of the ingredient density in the skin to the ingredient density outside the skin. (c) If the spray is reformulated so that the partition coefficient becomes very small, how long does the insect repellent remain effective?

A thick plate of pure iron at \(1000^{\circ} \mathrm{C}\) is subjected to a carburization process in which the surface of the plate is suddenly exposed to a gas that induces a carbon concentration \(C_{C, s}\) at one surface. The average diffusion coefficient for carbon and iron at this temperature is \(D_{\mathrm{C}-\mathrm{Fe}}=3 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}\). Use the correspondence between heat and mass transfer variables in addressing the following questions. (a) Consider the heat transfer analog to the carburization problem. Sketch the mass and heat transfer systems. Show and explain the correspondence between variables. Provide the analytical solutions to the heat and mass transfer problems. (b) Determine the carbon concentration ratio, \(C_{\mathrm{C}}(x, t) / C_{\mathrm{C}, s}\), at a depth of \(1 \mathrm{~mm}\) after \(1 \mathrm{~h}\) of carburization. (c) From the analogy, show that the time dependence of the mass flux of carbon into the plate may be expressed as \(n_{\mathrm{C}}^{\prime \prime}=\rho_{\mathrm{C}, s}\left(D_{\mathrm{C}-\mathrm{Fe}} / \pi t\right)^{1 / 2}\). Also, obtain an expression for the mass of carbon per unit area entering the iron plate over the time period \(t\).

A pharmaceutical product is designed to be absorbed in the gastrointestinal tract. The active ingredient is pressed into a tablet with a density of \(\rho_{\mathrm{A}}=15 \mathrm{~kg} / \mathrm{m}^{3}\) while the remainder of the tablet is composed of inactive ingredients. The partition coefficient is \(K=3 \times 10^{-2}\), and the diffusion coefficient of the active ingredient in the gastrointestinal fluid is \(D_{\mathrm{AB}}=0.4 \times 10^{-10} \mathrm{~m}^{2} / \mathrm{s}\). (a) Estimate the dosage delivered over a time period of \(5 \mathrm{~h}\) for a spherical tablet of diameter \(D=\) \(6 \mathrm{~mm}\). Hint: Assume the change in the tablet radius over the dosage period is small. (b) Estimate the dosage delivered over \(5 \mathrm{~h}\) for \(N=200\) small, spherical tablets contained in a gelatin capsule that quickly dissolves after ingestion, releasing the medication. The initial mass of the medication is the same as in part (a).

Consider combustion of hydrogen gas in a mixture of hydrogen and oxygen adjacent to the metal wall of a combustion chamber. Combustion occurs at constant temperature and pressure according to the chemical reaction \(2 \mathrm{H}_{2}+\mathrm{O}_{2} \rightarrow 2 \mathrm{H}_{2} \mathrm{O}\). Measurements under steady-state conditions at a distance of \(10 \mathrm{~mm}\) from the wall indicate that the molar concentrations of hydrogen, oxygen, and water vapor are \(0.10,0.10\), and \(0.20 \mathrm{kmol} / \mathrm{m}^{3}\), respectively. The generation rate of water vapor is \(0.96 \times 10^{-2} \mathrm{kmol} / \mathrm{m}^{3} \cdot \mathrm{s}\) throughout the region of interest. The binary diffusion coefficient for each of the species \(\left(\mathrm{H}_{2}, \mathrm{O}_{2}\right.\), and \(\left.\mathrm{H}_{2} \mathrm{O}\right)\) in the remaining species is \(0.6 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\). (a) Determine an expression for and make a qualitative plot of \(C_{\mathrm{H}_{2}}\) as a function of distance from the wall. (b) Determine the value of \(C_{\mathrm{H}_{2}}\) at the wall. (c) On the same coordinates used in part (a), sketch curves for the concentrations of oxygen and water vapor. (d) What is the molar flux of water vapor at \(x=10 \mathrm{~mm}\) ?

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