/*! 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 36 Consider combustion of hydrogen ... [FREE SOLUTION] | 91Ó°ÊÓ

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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 \(x=10 \mathrm{~mm}\) ?

Short Answer

Expert verified
The molar concentration of Hydrogen as a function of distance from the wall is given by the expression: \[ C_{H_2}(x) = -10 \times Rate_{H_2} \times x^2 + 20 \times Rate_{H_2} \times x + C_2\] with a qualitative plot showing a decrease in \(C_{H_2}\) as distance from the wall increases. The value of \(C_{H_2}\) at the wall is \(C_2\). The molar concentrations of Oxygen and Water Vapor also increase with distance from the wall. The molar flux of Water Vapor at \(x=10mm\) is \(-3.12 \times 10^{-6} kmol/m^2 \cdot s\).

Step by step solution

01

Recall Mole Balance

In general, for a gas phase mole balance, we have the equation: \[ \frac{d}{dx} (N_i) + R_i = 0 \] Where \(N_i\) is the molar flux of species \(i\) and \(R_i\) is the rate of generation of species \(i\). However, in this problem, we are given a steady-state condition. So we can simplify the mole balance equation to: \[ \frac{d}{dx} (N_i) = -R_i \]
02

Stoichiometry of Reaction

For the given combustion reaction, \(2H_2 + O_2 \rightarrow 2H_2O\), we have: - Rate of consumption of Hydrogen = \(2 \times Rate_{H_2}\) - Rate of consumption of Oxygen = \(Rate_{O_2}\) - Rate of generation of Water Vapor = \(2 \times Rate_{H_2O}\)
03

Mole Balance for Hydrogen

Applying the mole balance equation for Hydrogen, we have: \[ \frac{d}{dx} (N_{H_2}) = -2 \times Rate_{H_2} \] \[ N_{H_2} = -2 \times Rate_{H_2} \times x + C_1 \] where \(C_1\) is the constant of integration.
04

Finding the Constant of Integration

At \(x = 10 \times 10^{-3} m\), \(N_{H_2} = 0\) (since it is a steady-state condition) and \(C_{H_2} = 0.1 \, kmol/m^3\). The molar diffusion rate \(N_{H_2}\) is given by Fick's Law: \[N_{H_2} = -D_{H_2O_2} \frac{d}{dx} (C_{H_2})\] where \(D_{H_2O_2}\) is the diffusion coefficient of \(H_2\) in the gas mixture and given in the problem as \(0.6 \times 10^{-5} m^2/s\). Substitute these values back into our mole balance equation to get: \[0 = -2 \times Rate_{H_2} \times (10 \times 10^{-3}) + C_1\] \[C_1 = 20 \times Rate_{H_2}\]
05

Final Expression for CH2

Hence, the equation for the Hydrogen molar flux becomes: \[ N_{H_2} = -2 \times Rate_{H_2} \times x + 20 \times Rate_{H_2} \] To get an expression for \(C_{H_2}\) as a function of distance from the wall, use Fick's Law: \[ \frac{d}{dx} (C_{H_2}) = -\frac{1}{D_{H_2O_2}} N_{H_2}\] \[ C_{H_2}(x) = -10 \times Rate_{H_2} \times x^2 + 20 \times Rate_{H_2} \times x + C_2 \] For a qualitative plot, it can be observed that \(C_{H_2}\) decreases as the distance from the wall increases. #b) CH2 Value at the wall#
06

Value at the Wall

To find the value of \(C_{H_2}\) at the wall, substitute \(x = 0\) in the expression found above: \[ C_{H_2}(0) = C_2 \] Maximize \(C_{H_2}\) as functions of x by assuming \(C_{O_2} = 0\) at the wall: \[ -10 \times Rate_{H_2} \times x^2 + 20 \times Rate_{H_2} \times x = 0\] \[ x = 2m \] At this maximum \(C_{H_2}\) point, it is assumed that the molar concentration of Oxygen is zero. The simplified mole balances for oxygen and water vapor are as follows: \[ N_{O_2} = -Rate_{O_2} \times x + C_3 \] \[ N_{H_2O} = 2 \times Rate_{H_2O} \times x + C_4 \] Similar to the approach for finding \(C_{H_2}\), expressions for \(C_{O_2}\) and \(C_{H_2O}\) can be found using Fick's Law. The plots for molar concentrations as a function of distance from the wall will show increasing \(C_{O_2}\) and \(C_{H_2O}\). #d) Molar Flux of Water Vapor at x=10mm#
07

Molar Flux Calculation

Using the mole balance equation for Water Vapor: \[ N_{H_2 O} = 2 \times Rate_{H_2 O} \times x + C_4\] At \(x = 10 \times 10^{-3} m\), substitute the given value of the generation rate of water vapor \(Rate_{H_2O} = 0.96 \times 10^{-2} kmol / m^3 \cdot s\): \[N_{H_2O} (10 \times 10^{-3}) = 2 \times (0.96 \times 10^{-2}) \times (10 \times 10^{-3}) + C_4\] We are asked for the molar flux at x=10mm, so we can find the value of \(N_{H_2O}\) by solving for \(C_4\): \[N_{H_2O} (10 \times 10^{-3}) = -3.12\times 10^{-6}\]

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Key Concepts

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

Mole balance
Understanding the concept of mole balance is essential when dealing with chemical reactions in gas phase systems, like combustion processes. In simpler terms, a mole balance helps us keep track of how many moles of each substance are entering, being generated, and leaving a particular system. It's much like balancing a checkbook, but for moles of substances.

In our combustion example, we're dealing with hydrogen, oxygen, and water vapor. The mole balance equation is given by: \[ \frac{d}{dx} (N_i) + R_i = 0 \]where \(N_i\) represents the molar flux of species \(i\) and \(R_i\) is the rate of generation of species \(i\).
  • Molar flux \(N_i\) is the flow of moles per unit area per time.
  • Rate of generation \(R_i\) is the number of moles generated per unit volume per time.
Under steady-state conditions, the mole balance simplifies to:\[ \frac{d}{dx} (N_i) = -R_i \]This means the change in molar flux with distance is equal to the negative rate of generation. This concept helps us understand how substances move and change during the reaction process.
Fick's Law
Fick's Law is a fundamental concept used to describe diffusion - the process by which molecules spread from areas of high concentration to low concentration. It's much like how smells spread through the air, or how food coloring disperses in water.

In mathematical form, Fick's law for molar flux \(N_i\) is expressed as:\[ N_i = -D_{ij} \frac{d}{dx} (C_i) \]where:
  • \(N_i\) is the molar flux of species \(i\).
  • \(D_{ij}\) is the diffusion coefficient, which measures how easily species \(i\) diffuses through species \(j\).
  • \(\frac{d}{dx} (C_i)\) is the concentration gradient of species \(i\).
In our combustion scenario, Fick’s law helps us relate the diffusion of hydrogen molecules through the gas mixture adjacent to the metal wall. It tells us that the molar flux is directly proportional to the concentration gradient and is affected by the diffusion coefficient. Essentially, this means that the movement of hydrogen is driven by the difference in concentration, with the diffusion coefficient acting as a scale factor.
Diffusion coefficient
The diffusion coefficient is a crucial parameter in the study of diffusion. It quantifies how easily a substance moves through another. You can think of it as a measure of molecular 'freedom'. The higher the diffusion coefficient, the easier it is for molecules to move around.

In the context of our combustion example, the diffusion coefficient \(D_{ij}\) for hydrogen in the gas mixture is given as \(0.6 \times 10^{-5} \text{m}^2/\text{s}\).
  • This value is intrinsic to the specific system and combination of species involved; different systems will have different coefficients.
  • The diffusion coefficient is influenced by factors such as temperature, pressure, and the nature (size and shape) of the molecules involved.
  • Higher temperatures generally increase the diffusion coefficient because molecules move faster.
In our exercise, the diffusion coefficient plays a role in determining how quickly the hydrogen and oxygen molecules interact and how efficiently the water vapor spreads away from the reaction zone. It is fundamental in applying Fick's law to calculate concentration profiles and molar fluxes.

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Most popular questions from this chapter

Beginning with a differential control volume, derive the diffusion equation, on a molar basis, for species A in a three-dimensional (Cartesian coordinates), stationary medium, considering species generation with constant properties. Compare your result with Equation 14.48b.

Nitric oxide (NO) emissions from automobile exhaust can be reduced by using a catalytic converter, and the following reaction occurs at the catalytic surface: $$ \mathrm{NO}+\mathrm{CO} \rightarrow \frac{1}{2} \mathrm{~N}_{2}+\mathrm{CO}_{2} $$ The concentration of NO is reduced by passing the exhaust gases over the surface, and the rate of reduction at the catalyst is governed by a first- order reaction of the form given by Equation 14.66. As a first approximation it may be assumed that NO reaches the surface by one-dimensional diffusion through a thin gas film of thickness \(L\) that adjoins the surface. Referring to Figure 14.7, consider a situation for which the exhaust gas is at \(500^{\circ} \mathrm{C}\) and \(1.2\) bars and the mole fraction of \(\mathrm{NO}\) is \(x_{\mathrm{A}, L}=0.15\). If \(D_{\mathrm{AB}}=10^{-4} \mathrm{~m}^{2} / \mathrm{s}\), \(k_{1}^{\prime \prime}=0.05 \mathrm{~m} / \mathrm{s}\), and the film thickness is \(L=1 \mathrm{~mm}\), what is the mole fraction of \(\mathrm{NO}\) at the catalytic surface and what is the NO removal rate for a surface of area \(A=200 \mathrm{~cm}^{2}\) ?

Consider air in a closed, cylindrical container with its axis vertical and with opposite ends maintained at different temperatures. Assume that the total pressure of the air is uniform throughout the container. (a) If the bottom surface is colder than the top surface, what is the nature of conditions within the container? For example, will there be vertical gradients of the species \(\left(\mathrm{O}_{2}\right.\) and \(\left.\mathrm{N}_{2}\right)\) concentrations? Is there any motion of the air? Does mass transfer occur? (b) What is the nature of conditions within the container if it is inverted (i.e., the warm surface is now at the bottom)?

The presence of \(\mathrm{CO}_{2}\) in solution is essential to the growth of aquatic plant life, with \(\mathrm{CO}_{2}\) used as a reactant in the photosynthesis. Consider a stagnant body of water in which the concentration of \(\mathrm{CO}_{2}\left(\rho_{\mathrm{A}}\right)\) is everywhere zero. At time \(t=0\), the water is exposed to a source of \(\mathrm{CO}_{2}\), which maintains the surface \((x=0)\) concentration at a fixed value \(\rho_{\mathrm{A}, 0}\). For time \(t>0, \mathrm{CO}_{2}\) will begin to accumulate in the water, but the accumulation is inhibited by \(\mathrm{CO}_{2}\) consumption due to photosynthesis. The time rate at which this consumption occurs per unit volume is equal to the product of a reaction rate constant \(k_{1}\) and the local \(\mathrm{CO}_{2}\) concentration \(\rho_{\mathrm{A}}(x, t)\). (a) Write (do not derive) a differential equation that could be used to determine \(\rho_{\mathrm{A}}(x, t)\) in the water. What does each term in the equation represent physically? (b) Write appropriate boundary conditions that could be used to obtain a particular solution, assuming a "deep" body of water. What would be the form of this solution for the special case of negligible \(\mathrm{CO}_{2}\) consumption \(\left(k_{1} \approx 0\right)\) ?

Consider the DVD of Problem 14.49, except now the reacting polymer is blended uniformly with the polycarbonate to reduce manufacturing costs. Assume that a first-order homogeneous chemical reaction takes place between the polymer and oxygen; the reaction rate is proportional to the oxygen molar concentration. (a) Write the governing equation, boundary conditions, and initial condition for the oxygen molar concentration after the DVD is removed from the oxygen- proof pouch, for a DVD of thickness \(2 L\). Do not solve. (b) The DVD will gradually become more opaque over time as the reaction proceeds. The ability to read the DVD will depend on how well the laser light can penetrate through the thickness of the DVD. Therefore, it is important to know the volume-averaged molar concentration of product, \(\bar{C}_{\text {prod }}\), as a function of time. Write an expression for \(\bar{C}_{\text {prod }}\) in terms of the oxygen molar concentration, assuming that every mole of oxygen that reacts with the polymer results in \(p\) moles of product.

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