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Compound \(A\) diffuses through a 4 -cm-long tube and reacts as it diffuses. The equation governing diffusion with reaction is $$D \frac{d^{2} A}{d x^{2}}-k A=0$$ At one end of the tube, there is a large source of \(A\) at a concentration of \(0.1 \mathrm{M}\). At the other end of the tube there is an adsorbent material that quickly absorbs any \(A\), making the concentration \(0 \mathrm{M}\). If \(D=1.5 \times 10^{-6} \mathrm{cm}^{2 / \mathrm{s}}\) and \(k=5 \times 10^{-6} \mathrm{s}^{-1},\) what is the concentration of \(A\) as a function of distance in the tube?

Short Answer

Expert verified
The concentration of compound \(A\) as a function of distance in the tube is given by: \[A(x) = \frac{0.1 e^{\left(\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}}\right) (x-4)}}{e^{\left(2\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}}\right) 4} + 1}\]

Step by step solution

01

Rewriting the given equation

The given equation is $$D \frac{d^{2} A}{d x^{2}}-k A=0$$ First, we will divide both sides of the equation by \(D\) and simplify: \[\frac{d^{2} A}{d x^{2}}-\frac{k}{D} A=0\] Step 2: Guess the general solution
02

Guessing the general solution

With the simplified equation, we can guess the general solution has the form: $$A(x) = C_1 e^{mx} + C_2 e^{-mx}$$ where \(C_1\) and \(C_2\) are constants and \(m\) is a parameter that we will determine from the equation. Step 3: Obtain the particular solution
03

Obtaining the particular solution

Now, let's substitute the guess for the general solution into the simplified equation and solve for the parameter \(m\): \[\frac{d^{2} A(x)}{d x^{2}}-\frac{k}{D} A(x)=0\] \[\frac{d^2}{dx^2} (C_1 e^{mx} + C_2 e^{-mx}) - \frac{k}{D}(C_1 e^{mx} + C_2 e^{-mx}) = 0\] By taking the second derivative and plugging back into the equation, we find: $$m^2 = \frac{k}{D}\] So, \[m = \pm\sqrt{\frac{k}{D}}\] Now, we will use the boundary conditions to find the particular solution: At \(x=0\), \(A=0.1 \mathrm{M}\), so: \[A(0) = 0.1 = C_1 e^{0} + C_2 e^{0}\] Using the above equation, we obtain: \[C_1 + C_2 = 0.1\] At \(x=4\), \(A=0 \mathrm{M}\), so: \[A(4)=0 = C_1 e^{4m} + C_2 e^{-4m}\] Using the two boundary conditions, we can solve for \(C_1\) and \(C_2\). Step 4: Solve for constants
04

Solving for constants \(C_1\) and \(C_2\)

With the two boundary conditions, we obtain a system of linear equations for \(C_1\) and \(C_2\): \[\begin{cases} C_1 + C_2 = 0.1 \\ C_1 e^{4m} + C_2 e^{-4m} = 0 \end{cases}\] Solving for \(C_1\) and \(C_2\), we get: \[C_1 = \frac{0.1}{e^{4m} + e^{-4m}}\] \[C_2 = 0.1-C_1\] Step 5: Final concentration as a function of distance
05

Finding the concentration of \(A\) as a function of distance

With the values of constants \(C_1\) and \(C_2\), let's substitute these back into the general solution along with the given values of \(D\) and \(k\): \[A(x) = \frac{0.1}{e^{\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}} \cdot 4} + e^{-\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}} \cdot 4}} e^{\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}} \cdot x} + (0.1-\frac{0.1}{e^{\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}} \cdot 4} + e^{-\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}} \cdot 4}}) e^{-\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}} \cdot x}\] Simplifying the equation gives the concentration of A as a function of distance in the tube: \[A(x) = \frac{0.1 e^{\left(\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}}\right) (x-4)}}{e^{\left(2\sqrt{\frac{5 \times 10^{-6}}{1.5 \times 10^{-6}}}\right) 4} + 1}\]

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Key Concepts

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

Boundary Conditions
In differential equation problems, boundary conditions are the additional pieces of information provided to find a particular solution. They describe how the system behaves at certain points, typically at the boundaries of the domain. In the given exercise, boundary conditions are used to solve for constants in the concentration equation of compound \( A \).

Here are the boundary conditions for diffusion through the tube:
  • At \( x = 0 \), the concentration \( A \) is 0.1 M, as this end of the tube is adjacent to the large source of \( A \).
  • At \( x = 4 \), the concentration \( A \) becomes 0 M, due to the presence of an adsorbent material that removes any remaining \( A \).
To solve the differential equation, these conditions help determine specific values for any arbitrary constants found in the general solution. By applying the boundary conditions, we achieve a "tailored" solution that fits the described physical scenario. This means our solution accurately reflects the reality of the tube's behavior at its endpoints.
Concentration Gradient
The concentration gradient describes how the concentration of compound \( A \) changes as it diffuses through the tube. This gradient is a crucial part of understanding diffusion processes, especially when reactions occur simultaneously, as in this exercise.

The concentration difference is highest near the source of \( A \), where it starts at 0.1 M, and declines to 0 M toward the adsorbent end. This decline can be represented graphically by a smooth curve that tails off as it moves away from the source. The concentration gradient is effectively a slope in the direction of decreasing concentration.
  • Higher gradients indicate a stronger driving force for diffusion, meaning \( A \) will diffuse more rapidly to areas of lower concentration.
  • Lower gradients suggest slower diffusion, as the "push" for \( A \) to move is less intense.
Understanding the gradient and its mathematical description through the solved equation helps us predict how quickly the compound will distribute itself throughout the tube and ensures we navigate any potential implications for reactions or processes that depend on this distribution.
Second Order Differential Equation
The exercise involves a second order differential equation, which signifies that the highest derivative in the equation is of the second degree. This type of equation is common in expressing physical phenomena such as diffusion processes. Here, we focus on the diffusion of compound \( A \) as it reacts within the tube.

Second order differential equations are important because they can model more complex dynamics that simple, first-order equations cannot. In the provided exercise, the framework is:

\[ D \frac{d^{2} A}{d x^{2}} - k A = 0 \]This equation includes a term with the second derivative \( \frac{d^{2} A}{d x^{2}} \) which reflects how the concentration of \( A \) accelerates and changes as a function of position within the tube.
  • The parameter \( D \) stands for the diffusion coefficient, showing how quickly \( A \) spreads through the tube.
  • \( k \) represents a reaction rate constant, incorporating the speed at which \( A \) reacts as it diffuses.
Solving such an equation usually involves finding the general solution, assuming a particular form for the solution (based on characteristics of the equation), and then applying boundary conditions to reduce ambiguity. Errors are less likely when these steps are executed correctly, providing us with a precise concentration profile of \( A \) throughout the tube.

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Most popular questions from this chapter

In the investigation of a homicide or accidental death, it is often important to estimate the time of death. From the experimental observations, it is known that the surface temperature of an object changes at a rate proportional to the difference between the temperature of the object and that of the surrounding environment or ambient temperature. This is known as Newton's law of cooling. Thus, if \(T(t)\) is the temperature of the object at time \(t,\) and \(T_{a}\) is the constant ambient temperature: $$\frac{d T}{d t}=-K\left(T-T_{a}\right)$$ where \(K>0\) is a constant of proportionality. Suppose that at time \(t=0\) a corpse is discovered and its temperature is measured to be \(T_{o}\) We assume that at the time of death, the body temperature, \(T_{d}\) was at the normal value of \(37^{\circ} \mathrm{C}\). Suppose that the temperature of the corpse when it was discovered was \(29.5^{\circ} \mathrm{C}\), and that two hours later, it is \(23.5^{\circ} \mathrm{C}\). The ambient temperature is \(20^{\circ} \mathrm{C}\) (a) Determine \(K\) and the time of death. (b) Solve the ODE numerically and plot the results.

A biofilm with a thickness, \(L_{f}[\mathrm{cm}]\), grows on the surface of a solid (Fig. \(P 28.13\) ). After traversing a diffusion layer of thickness, \(L[\mathrm{cm}],\) a chemical compound, \(A,\) diffuses into the biofilm where it is subject to an irreversible first-order reaction that converts it to a product, \(B\) Steady-state mass balances can be used to derive the following ordinary differential equations for compound \(A\) : $$\begin{aligned} &D \frac{d^{2} c_{a}}{d x^{2}}=0 \quad 0 \leq x

The following ODEs have been proposed as a model of an epidemic: \\[ \begin{array}{l} \frac{d S}{d t}=-a S I \\ \frac{d I}{d t}=a S I-r I \\ \frac{d R}{d t}=r I \end{array} \\] where \(S=\) the susceptible individuals, \(I=\) the infected, \(R=\) the recovered, \(a=\) the infection rate, and \(r=\) the recovery rate. A city has 10,000 people, all of whom are susceptible. (a) If a single infectious individual enters the city at \(t=0\) compute the progression of the epidemic until the number of infected individuals falls below \(10 .\) Use the following parameters: \(a=0.002 /\) (person \(\cdot\) week ) and \(r=0.15 /\) d. Develop time series plots of all the state variables. Also generate a phase plane plot of \(S\) versus \(I\) versus \(R\) (b) Suppose that after recovery, there is a loss of immunity that causes recovered individuals to become susceptible. This reinfection mechanism can be computed as \(\rho R,\) where \(\rho=\) the reinfection rate. Modify the model to include this mechanism and repeat the computations in (a) using \(\rho=0.015 / \mathrm{d}\).

A spherical ice cube (an "ice sphere") that is \(6 \mathrm{cm}\) in diameter is removed from a \(0^{\circ} \mathrm{C}\) freezer and placed on a mesh screen at room temperature \(T_{a}=20^{\circ} \mathrm{C} .\) What will be the diameter of the ice cube as a function of time out of the freezer (assuming that all the water that has melted immediately drips through the screen)? The heat transfer coefficient \(h\) for a sphere in a still room is about \(3 \mathrm{W} /\left(\mathrm{m}^{2} \cdot \mathrm{K}\right) .\) The heat flux from the ice sphere to the air is given by $$\mathrm{Flux}=\frac{q}{A}=h\left(T_{\mathrm{a}}-T\right)$$ where \(q=\) heat and \(A=\) surface area of the sphere. Use a numerical method to make your calculation. Note that the latent heat of fusion is \(333 \mathrm{kJ} / \mathrm{kg}\) and the density of ice is approximately \(0.917 \mathrm{kg} / \mathrm{m}^{3}\).

\(\mathrm{A}\) mass balance for a chemical in a completely mixed reactor can be written as \\[ V \frac{d c}{d t}=F-Q c-k V c^{2} \\] where \(V=\) volume \(\left(12 \mathrm{m}^{3}\right), c=\) concentration \(\left(\mathrm{g} / \mathrm{m}^{3}\right), F=\) feed rate \((175 \mathrm{g} / \mathrm{min}), Q=\) flow rate \(\left(1 \mathrm{m}^{3} / \mathrm{min}\right),\) and \(k=\mathrm{a}\) second-order reaction rate \(\left(0.15 \mathrm{m}^{3} / \mathrm{g} / \mathrm{min}\right) .\) If \(c(0)=0,\) solve the ODE until the concentration reaches a stable level. Use the midpoint method \((h=0.5)\) and plot your results. Challenge question: If one ignores the fact that concentrations must be positive, find a range of initial conditions such that you obtain a very different trajectory than was obtained with \(c(0)=0\) Relate your results to the steady-state solutions.

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