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Fundamentals of Heat and Mass Transfer

Theodore L. Bergman, Adrienne S. Lavine, Frank P. Incropera

Chapter 14

Diffusion Mass Transfer - all with Video Answers

Educators


Chapter Questions

01:49

Problem 1

Assuming air to be composed exclusively of $\mathrm{O}_{2}$ and $\mathrm{N}_{2}$, with their partial pressures in the ratio $0.21: 0.79$, what are their mass fractions?

Marissa Turner
Marissa Turner
Numerade Educator
09:55

Problem 2

Consider an ideal gas mixture of $n$ species.
(a) Derive an equation for determining the mass fraction of species $i$ from knowledge of the mole fraction and the molecular weight of each of the $n$ species. Derive an equation for determining the mole fraction of species $i$ from knowledge of the mass fraction and the molecular weight of each of the $n$ species.
(b) In a mixture containing equal mole fractions of $\mathrm{O}_{2}$, $\mathrm{N}_{2}$, and $\mathrm{CO}_{2}$, what is the mass fraction of each species? In a mixture containing equal mass fractions of $\mathrm{O}_{2}, \mathrm{~N}_{2}$, and $\mathrm{CO}_{2}$, what is the mole fraction of each species?

Aparna Shakti
Aparna Shakti
Numerade Educator
09:55

Problem 3

A mixture of $\mathrm{CO}_{2}$ and $\mathrm{N}_{2}$ is in a container at $25^{\circ} \mathrm{C}$, with each species having a partial pressure of 1 bar. Calculate the molar concentration, the mass density, the mole fraction, and the mass fraction of each species.

Aparna Shakti
Aparna Shakti
Numerade Educator
02:05

Problem 4

A He-Xe mixture containing $0.75$ mole fraction of helium is used for cooling of electronics in an avionics application. At a temperature of $300 \mathrm{~K}$ and atmospheric pressure, calculate the mass fraction of helium and the mass density, molar concentration, and molecular weight of the mixture. If the cooling system capacity is $10 \mathrm{~L}$, what is the mass of the coolant?

John Nicolle
John Nicolle
Numerade Educator
06:22

Problem 5

Estimate values of the mass diffusivity $D_{\mathrm{AB}}$ for binary mixtures of the following gases at $350 \mathrm{~K}$ and $1 \mathrm{~atm}$ : ammonia-air and hydrogen-air.

Niamat Khuda
Niamat Khuda
Numerade Educator
02:03

Problem 6

Plot the mass diffusivity, $D_{\mathrm{AB}}$, versus the molecular weight of Substance A for Substance B being air at $p=1.5 \mathrm{~atm}, T=320 \mathrm{~K}$. Substance $\mathrm{A}$ is each of the first 8 entries of Table A.8. Is your plot consistent with kinetic theory? Consult various sources, including Table A.4 and Example $6.2$ for molecular weight values.

Akshaya Rs
Akshaya Rs
Numerade Educator
01:45

Problem 7

A 100-mm-long, hollow iron cylinder is exposed to a $1000^{\circ} \mathrm{C}$ carburizing gas (a mixture of $\mathrm{CO}$ and $\mathrm{CO}_{2}$ ) at its inner and outer surfaces of radii $4.30$ and $5.70 \mathrm{~mm}$, respectively. Consider steady-state conditions for which carbon diffuses from the inner surface of the iron wall to the outer surface and the total transport amounts to $3.6 \times 10^{-3} \mathrm{~kg}$ of carbon over $100 \mathrm{~h}$. The variation of the carbon composition (weight $\%$ carbon) with radius is tabulated for selected radii.
$$
\begin{array}{lllllllll}
r(\mathrm{~mm}) & 4.49 & 4.66 & 4.79 & 4.91 & 5.16 & 5.27 & 5.40 & 5.53 \\
\text { Wt.C }(\%) & 1.42 & 1.32 & 1.20 & 1.09 & 0.82 & 0.65 & 0.46 & 0.28
\end{array}
$$
(a) Beginning with Fick's law and the assumption of a constant diffusion coefficient, $D_{\mathrm{C}-\mathrm{Fe}}$, show that $d \rho_{\mathrm{C}} / d(\ln r)$ is a constant. Sketch the carbon mass density, $\rho_{\mathrm{C}}(r)$, as a function of $\ln r$ for such a diffusion process.
(b) The foregoing table corresponds to measured distributions of the carbon mass density. Is $D_{\mathrm{C}-\mathrm{Fe}}$ constant for this diffusion process? If not, does $D_{\mathrm{C}-\mathrm{Fe}}$ increase or decrease with an increasing carbon concentration?
(c) Using the experimental data, calculate and tabulate $D_{\mathrm{C}-\mathrm{Fe}}$ for selected carbon compositions.

Manik Pulyani
Manik Pulyani
Numerade Educator
14:40

Problem 8

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)?

Yaqub Khan
Yaqub Khan
Numerade Educator
05:08

Problem 9

An old-fashioned glass apothecary jar contains a patent medicine. The neck is closed with a rubber stopper that is $20 \mathrm{~mm}$ tall, with a diameter of $10 \mathrm{~mm}$ at the bottom end, widening to $20 \mathrm{~mm}$ at the top end. The molar concentration of medicine vapor in the stopper is $2 \times 10^{-3} \mathrm{kmol} / \mathrm{m}^{3}$ at the bottom surface and is negligible at the top surface. If the mass diffusivity of medicine vapor in rubber is $0.2 \times 10^{-9} \mathrm{~m}^{2} / \mathrm{s}$, find the rate $(\mathrm{kmol} / \mathrm{s})$ at which vapor exits through the stopper.

Amy Jiang
Amy Jiang
Numerade Educator
03:29

Problem 10

Consider the evaporation of liquid A into a column containing a binary gas mixture of $\mathrm{A}$ and $\mathrm{B}$. Species $B$ cannot be absorbed in liquid $A$ and the boundary conditions are the same as in Section 14.2.2. Show how the ratio of the molar-average velocity to the species velocity of $\mathrm{A}, v_{x}^{*} / v_{\mathrm{A}, x}$, varies with the mole fraction of species A.

Nicole Smina
Nicole Smina
Numerade Educator
11:15

Problem 11

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.

Chareen Guzman
Chareen Guzman
Numerade Educator
03:46

Problem 12

A spherical droplet of liquid $\mathrm{A}$ and radius $r_{o}$ evaporates into a stagnant layer of gas B. Derive an expression for the evaporation rate of species $A$ in terms of the saturation pressure of species $\mathrm{A}, p_{\mathrm{A}}\left(r_{o}\right)=p_{\mathrm{A} \text { sall }}$, the partial pressure of species $\mathrm{A}$ at an arbitrary radius $r$, $p_{\mathrm{A}}(r)$, the total pressure $p$, and other pertinent quantities. Assume the droplet and the mixture are at a uniform pressure $p$ and temperature $T$.

Chai Santi
Chai Santi
Numerade Educator
01:22

Problem 13

The presence of a small amount of air may cause a significant reduction in the heat rate to a water-cooled steam condenser surface. For a clean surface with pure steam and the prescribed conditions, the condensate rate is $0.020 \mathrm{~kg} / \mathrm{m}^{2} \cdot \mathrm{s}$. With the presence of stagnant air in the steam, the condensate surface temperature drops from 28 to $24^{\circ} \mathrm{C}$ and the condensate rate is reduced by a factor of 2 . For the air-steam mixture, determine the partial pressure of air as a function of distance from the condensate film.

Hast Aggarwal
Hast Aggarwal
Numerade Educator
20:05

Problem 14

A laboratory apparatus to measure the diffusion coefficient of vapor-gas mixtures consists of a vertical, small-diameter column containing the liquid phase that evaporates into the gas flowing over the mouth of the column. The gas flow rate is sufficient to maintain a negligible vapor concentration at the exit plane. The column is $150 \mathrm{~mm}$ high, and the pressure and temperature in the chamber are maintained at $0.25$ atm and $320 \mathrm{~K}$, respectively. For calibration purposes, you've been asked to calculate the expected evaporation rate $\left(\mathrm{kg} / \mathrm{h} \cdot \mathrm{m}^{2}\right)$ for a test with water and air under the foregoing conditions, using the known value of $D_{\mathrm{AB}}$ for the vapor-air mixture.

Chareen Guzman
Chareen Guzman
Numerade Educator
03:04

Problem 15

A thin plastic membrane is used to separate helium from a gas stream. Under steady-state conditions the concentration of helium in the membrane is known to be $0.02$ and $0.005 \mathrm{kmol} / \mathrm{m}^{3}$ at the inner and outer surfaces, respectively. If the membrane is $1 \mathrm{~mm}$ thick and the binary diffusion coefficient of helium with respect to the plastic is $10^{-9} \mathrm{~m}^{2} / \mathrm{s}$, what is the diffusive flux?

Ameer Said
Ameer Said
Numerade Educator
01:37

Problem 16

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.

Penny Riley
Penny Riley
Numerade Educator
01:37

Problem 17

Consider the radial diffusion of a gaseous species (A) through the wall of a plastic tube (B), and allow for chemical reactions that provide for the depletion of A at a rate $\dot{N}_{\mathrm{A}}\left(\mathrm{kmol} / \mathrm{s} \cdot \mathrm{m}^{3}\right)$. Derive a differential equation that governs the molar concentration of species A in the plastic.

Penny Riley
Penny Riley
Numerade Educator
01:37

Problem 18

Beginning with a differential control volume, derive the diffusion equation, on a molar basis, for species A in a one-dimensional, spherical, stationary medium, considering species generation. Compare your result with Equation 14.50.

Penny Riley
Penny Riley
Numerade Educator
19:42

Problem 19

Gaseous hydrogen at 10 bars and $27^{\circ} \mathrm{C}$ is stored in a 100 -mm-diameter spherical tank having a steel wall $2 \mathrm{~mm}$ thick. The molar concentration of hydrogen in the steel is $1.50 \mathrm{kmol} / \mathrm{m}^{3}$ at the inner surface and negligible at the outer surface, while the diffusion coefficient of hydrogen in steel is approximately $0.3 \times 10^{-12} \mathrm{~m}^{2} / \mathrm{s}$. What is the initial rate of mass loss of hrogen by diffusion through the tank wall? What is the initial rate of pressure drop within the tank?

Chareen Guzman
Chareen Guzman
Numerade Educator
03:57

Problem 20

Consider the interface between atmospheric air and a body of water, both at $17^{\circ} \mathrm{C}$.
(a) What are the mole and mass fractions of water at the air side of the interface? At the water side of the interface?
(b) What are the mole and mass fractions of oxygen at the air side of the interface? At the water side of the interface? The atmospheric air may be assumed to contain $20.5 \%$ oxygen by volume.

Mahnoor Amin
Mahnoor Amin
Numerade Educator
19:42

Problem 21

Hydrogen at a pressure of 2 atm flows within a tube of diameter $40 \mathrm{~mm}$ and wall thickness $0.5 \mathrm{~mm}$. The outer surface is exposed to a gas stream for which the hydrogen partial pressure is $0.1 \mathrm{~atm}$. The mass diffusivity and solubility of hydrogen in the tube material are $1.8 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}$ and $160 \mathrm{kmol} / \mathrm{m}^{3}$ *atm, respectively. When the system is at $500 \mathrm{~K}$, what is the rate of hydrogen transfer through the tube per unit length $(\mathrm{kg} / \mathrm{s} \cdot \mathrm{m})$ ?

Chareen Guzman
Chareen Guzman
Numerade Educator
02:08

Problem 22

Oxygen gas is maintained at pressures of 2 bars and 1 bar on opposite sides of a rubber membrane that is $0.5 \mathrm{~mm}$ thick, and the entire system is at $25^{\circ} \mathrm{C}$. What is the molar diffusive flux of $\mathrm{O}_{2}$ through the membrane? What are the molar concentrations of $\mathrm{O}_{2}$ on both sides of the membrane (outside the rubber)?

Nadia Lara
Nadia Lara
Numerade Educator
02:59

Problem 23

Insulation degrades (experiences an increase in thermal conductivity) if it is subjected to water vapor condensation. The problem may occur in home insulation during cold periods, when vapor in a humidified room diffuses through the drywall (plaster board) and condenses in the adjoining insulation. Estimate the mass diffusion rate for a $3 \mathrm{~m} \times 5 \mathrm{~m}$ wall, under conditions for which the vapor pressure is $0.03$ bar in the room air and $0.0$ bar in the insulation. The drywall is $10 \mathrm{~mm}$ thick, and the solubility of water vapor in the wall material is approximately $5 \times 10^{-3} \mathrm{kmol} / \mathrm{m}^{3}$ - bar. The binary diffusion coefficient for water vapor in the drywall is approximately $10^{-9} \mathrm{~m}^{2} / \mathrm{s}$.

Manish Jain
Manish Jain
Numerade Educator
02:11

Problem 24

Helium gas at $25^{\circ} \mathrm{C}$ and 4 bars is contained in a glass cylinder of $100-\mathrm{mm}$ inside diameter and $5-\mathrm{mm}$ thickness. What is the rate of mass loss per unit length of the cylinder?

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
05:27

Problem 25

Helium gas at $25^{\circ} \mathrm{C}$ and 4 bars is stored in a spherical Pyrex container of $200-\mathrm{mm}$ inside diameter and 10 $\mathrm{mm}$ thickness. What is the rate of mass loss from the container?

Alick Cushing
Alick Cushing
Numerade Educator
01:34

Problem 26

Consider the blister packaging material of Example 14.3.
(a) Under the same conditions as in the example, determine the solubility of the polymer material ( $\mathrm{kmol} / \mathrm{m}^{3}$ - bar) if the temperature is $295 \mathrm{~K}$ and the relative humidity inside and outside the package is $\phi_{2}=0.1$ and $\phi_{1}=0.9$, respectively.
(b) By selecting a different packaging material, the diffusivity of the film may be changed. Determine the total water vapor transfer rate associated with reducing the diffusivity to $10 \%$ of its original value.
(c) The solubility of the material adjacent to its exposed surface may be modified by coating it with various thin films. Determine the water vapor transfer rate after coating both sides of the original polymer sheet and, in turn, reducing the solubility near both surfaces to $10 \%$ of the original value.
(d) Determine the water vapor transfer rate after coating the exterior of the original polymer sheet and reducing its solubility by a factor of 9 , while leaving the interior surface untreated.

Manik Pulyani
Manik Pulyani
Numerade Educator
07:10

Problem 27

An experiment is designed to measure the partition coefficient, $K$, associated with the transfer of a pharmaceutical product through a polymer material. The partition coefficient is defined as the ratio of the densities of the species of interest (the pharmaceutical) on either side of an interface. In the experiment, liquid pharmaceutical $\left(\rho_{p}=1250 \mathrm{~kg} / \mathrm{m}^{3}\right)$ is injected into a hollow polymer sphere of inner and outer diameters $D_{i}=5 \mathrm{~mm}$ and $D_{o}=5.1 \mathrm{~mm}$, respectively. The sphere is exposed to convective conditions for which the density of the pharmaceutical at the outer surface is zero. After one week, the sphere's mass is reduced by $\Delta M=8.2 \mathrm{mg}$. What is the value of the partition coefficient if the mass diffusivity is $D_{\mathrm{AB}}=0.2 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}$ ?

Sachin Rao
Sachin Rao
Numerade Educator
01:41

Problem 28

Ultra-pure hydrogen is required in applications ranging from the manufacturing of semiconductors to powering fuel cells. The crystalline structure of palladium allows only the transfer of atomic hydrogen (H) through its thickness, and therefore palladium membranes are used to filter hydrogen from contaminated streams containing mixtures of hydrogen and other gases. Hydrogen molecules $\left(\mathrm{H}_{2}\right)$ are first adsorbed onto the palladium's surface and are then dissociated into atoms $(\mathrm{H})$, which subsequently diffuse through the metal. The H atoms recombine on the opposite side of the membrane, forming pure $\mathrm{H}_{2}$. The surface concentration of H takes the form $C_{\mathrm{H}}=K_{s} p_{\mathrm{H}_{2}}^{05}$, where $K_{s} \approx$ $1.4 \mathrm{kmol} / \mathrm{m}^{3} \cdot \mathrm{bar}^{0.5}$ is known as Sieverts constant. Consider an industrial hydrogen purifier consisting of an array of palladium tubes with one tube end connected to a collector plenum and the other end closed. The tube bank is inserted into a shell. Impure $\mathrm{H}_{2}$ at $T=$ $600 \mathrm{~K}, p=15$ bars, $x_{\mathrm{H}_{2}}=0.85$ is introduced into the shell while pure $\mathrm{H}_{2}$ at $p=6$ bars, $T=600 \mathrm{~K}$ is extracted through the tubes. Determine the production rate of pure hydrogen $(\mathrm{kg} / \mathrm{h})$ for $N=100$ tubes which are of inside diameter $D_{i}=1.6 \mathrm{~mm}$, wall thickness $t=75 \mu \mathrm{m}$, and length $L=80 \mathrm{~mm}$. The mass diffusivity of hydrogen $(\mathrm{H})$ in palladium at $600 \mathrm{~K}$ is approximately $D_{\mathrm{AB}}=7 \times 10^{-9} \mathrm{~m}^{2} / \mathrm{s}$.

Arpit Gupta
Arpit Gupta
Numerade Educator
01:14

Problem 29

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 $A=200 \mathrm{~cm}^{2}$ ?

MP
Mihir Paranjape
Numerade Educator
01:53

Problem 30

Pulverized coal pellets, which may be approximated as carbon spheres of radius $r_{o}=1 \mathrm{~mm}$, are burned in a pure oxygen atmosphere at $1450 \mathrm{~K}$ and 1 atm. Oxygen is transferred to the particle surface by diffusion, where it is consumed in the reaction $\mathrm{C}+\mathrm{O}_{2} \rightarrow \mathrm{CO}_{2}$. The reaction rate is first order and of the form $\dot{N}_{\mathrm{O}_{2}}^{\prime \prime}=$ $-k_{1}^{\prime \prime} C_{\mathrm{O}_{2}}\left(r_{o}\right)$, where $k_{1}^{\prime \prime}=0.1 \mathrm{~m} / \mathrm{s}$. Neglecting changes in $r_{o}$, determine the steady-state $\mathrm{O}_{2}$ molar consumption rate in $\mathrm{kmol} / \mathrm{s}$. At $1450 \mathrm{~K}$, the binary diffusion coefficient for $\mathrm{O}_{2}$ and $\mathrm{CO}_{2}$ is $1.71 \times 10^{-4} \mathrm{~m}^{2} / \mathrm{s}$.

Manik Pulyani
Manik Pulyani
Numerade Educator
05:17

Problem 31

To enhance the effective surface, and hence the chemical reaction rate, catalytic surfaces often take the form of porous solids. One such solid may be visualized as consisting of a large number of cylindrical pores, each of diameter $D$ and length $L$.
To enhance the effective surface, and hence the chemical reaction rate, catalytic surfaces often take the form of porous solids. One such solid may be visualized as consisting of a large number of cylindrical pores, each of diameter $D$ and length $L$. Consider conditions involving a gaseous mixture of $\mathrm{A}$ and B for which species A is chemically consumed at the catalytic surface. The reaction is known to be first order, and the rate at which it occurs per unit area of the surface may be expressed as $k_{1}^{\prime \prime} C_{\mathrm{A}}$, where $k_{1}^{\prime \prime}(\mathrm{m} / \mathrm{s})$ is the reaction rate constant and $C_{\mathrm{A}}\left(\mathrm{kmol} / \mathrm{m}^{3}\right)$ is the local molar concentration of species A. Under steadystate conditions, flow over the porous solid is known to maintain a fixed value of the molar concentration $C_{\mathrm{A}, 0}$ at the pore mouth. Beginning from fundamentals, obtain the differential equation that governs the variation of $C_{\mathrm{A}}$ with distance $x$ along the pore. Applying appropriate boundary conditions, solve the equation to obtain an expression for $C_{\mathrm{A}}(x)$.

Eric Mockensturm
Eric Mockensturm
Numerade Educator
02:17

Problem 32

A platinum catalytic reactor in an automobile is used to convert carbon monoxide to carbon dioxide in an oxidation reaction of the form $2 \mathrm{CO}+\mathrm{O}_{2} \rightarrow 2 \mathrm{CO}_{2}$. Species transfer between the catalytic surface and the exhaust gases may be assumed to occur by diffusion in a film of thickness $L=10 \mathrm{~mm}$. Consider an exhaust gas that has a pressure of $1.2$ bars, a temperature of $500^{\circ} \mathrm{C}$, and a $\mathrm{CO}$ mole fraction of $0.0012$. If the reaction rate constant of the catalyst is $k_{1}^{\prime \prime}=0.005 \mathrm{~m} / \mathrm{s}$ and the diffusion coefficient of $\mathrm{CO}$ in the mixture is $10^{-4} \mathrm{~m}^{2} / \mathrm{s}$, what is the molar concentration of $\mathrm{CO}$ at the catalytic surface? What is the rate of removal of $\mathrm{CO}$ per unit area of the catalyst? What is the removal rate if $k_{1}^{\prime \prime}$ is adjusted to render the process diffusion limited?

David Collins
David Collins
Numerade Educator
06:28

Problem 33

A novel process has been proposed to create a composite palladium tube for use as a hydrogen separation membrane in order to produce high-purity hydrogen. To fabricate the composite palladium tube, a gas containing palladium (species A) flows through a porouswalled tube, and the palladium deposits into the pores of the tube wall. The gas mass flow rate is $\dot{m}$ and the inlet mass concentration of palladium is $\rho_{\mathrm{A}, m, i}$. The mass transfer coefficient for transfer of palladium between the gas and the surface is $h_{m}$, and the deposition rate is proportional to the mass concentration of palladium at the tube surface, that is, $-n_{\mathrm{A}, s}^{\prime \prime}=k_{1} \rho_{\mathrm{A}, s}$. The palladium is a dilute species, so the total mass flow rate is approximately constant down the length of the tube.
(a) Building upon the convection mass transfer analysis presented in Section 8.9, derive an expression for the variation of the mean species density of palladium with distance from the tube entrance, and determine an expression for the local deposition rate $\left(\mathrm{kg} / \mathrm{m}^{2} \cdot \mathrm{s}\right)$ for a tube of diameter D. Neglect any leakage of gas through the porous tube walls.
(b) If the tube is too long, the variation in deposit thickness will be unacceptably large. What is the ratio of the deposition rates at $x=L$ and $x=0$ ?

Averell Hause
Averell Hause
Carnegie Mellon University
02:51

Problem 34

Consider a spherical organism of radius $r_{o}$ within which respiration occurs at a uniform volumetric rate of $\dot{N}_{\mathrm{A}}=-k_{0}$. That is, oxygen (species A) consumption is governed by a zero-order, homogeneous chemical reaction.
(a) If a molar concentration of $C_{\mathrm{A}}\left(r_{o}\right)=C_{\mathrm{A}, o}$ is maintained at the surface of the organism, obtain an expression for the radial distribution of oxygen, $C_{\mathrm{A}}(r)$, within the organism. From your solution, can you discern any limits on applicability of the result?
(b) Obtain an expression for the rate of oxygen consumption within the organism.
(c) Consider an organism of radius $r_{o}=0.10 \mathrm{~mm}$ and a diffusion coefficient for oxygen transfer of $D_{\mathrm{AB}}=10^{-8} \mathrm{~m}^{2} / \mathrm{s}$. If $C_{\mathrm{A}, o}=5 \times 10^{-5} \mathrm{kmol} / \mathrm{m}^{3}$and $k_{0}=1.2 \times 10^{-4} \mathrm{kmol} / \mathrm{s}^{*} \mathrm{~m}^{3}$, what is the molar concentration of $\mathrm{O}_{2}$ at the center of the organism?

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
18:44

Problem 35

Referring to Problem 14.34, a more representative model of respiration in a spherical organism is one for which oxygen consumption is governed by a firstorder reaction of the form $\dot{N}_{\mathrm{A}}=-k_{1} C_{\mathrm{A}}$.
(a) If a molar concentration of $C_{\mathrm{A}}\left(r_{o}\right)=C_{\mathrm{A}, o}$ is maintained at the surface of the organism, obtain an expression for the radial distribution of oxygen, $C_{\mathrm{A}}(r)$, within the organism. Hint: To simplify solution of the species diffusion equation, invoke the transformation $y \equiv r C_{\mathrm{A}}$.
(b) Obtain an expression for the rate of oxygen consumption within the organism.
(c) Consider an organism of radius $r_{o}=0.10 \mathrm{~mm}$ and a diffusion coefficient of $D_{\mathrm{AB}}=10^{-8} \mathrm{~m}^{2} / \mathrm{s}$. If $C_{\mathrm{A}, o}=5 \times 10^{-5} \mathrm{kmol} / \mathrm{m}^{3}$ and $k_{1}=20 \mathrm{~s}^{-1}$, estimate the corresponding value of the molar concentration at the center of the organism. What is the rate of oxygen consumption by the organism?

Daniel Azubuike
Daniel Azubuike
Numerade Educator
01:25

Problem 36

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 $x=10 \mathrm{~mm}$ ?

Hast Aggarwal
Hast Aggarwal
Numerade Educator
02:51

Problem 37

Consider the problem of oxygen transfer from the interior lung cavity, across the lung tissue, to the network of blood vessels on the opposite side. The lung tissue (species B) may be approximated as a plane wall of thickness $L$. The inhalation process may be assumed to maintain a constant molar concentration $C_{\mathrm{A}}(0)$ of oxygen (species A) in the tissue at its inner surface $(x=0)$, and assimilation of oxygen by the blood may be assumed to maintain a constant molar concentration $C_{\mathrm{A}}(L)$ of oxygen in the tissue at its outer surface $(x=L)$. There is oxygen consumption in the tissue due to metabolic processes, and the reaction is zero order, with $\dot{N}_{\mathrm{A}}=-k_{0}$. Obtain expressions for the distribution of the oxygen concentration in the tissue and for the rate of assimilation of oxygen by the blood per unit tissue surface area.

Khoobchandra Agrawal
Khoobchandra Agrawal
Numerade Educator
03:37

Problem 38

As an employee of the Los Angeles Air Quality Commission, you have been asked to develop a model for computing the distribution of $\mathrm{NO}_{2}$ in the atmosphere. The molar flux of $\mathrm{NO}_{2}$ at ground level, $N_{\mathrm{A}, 0}^{N}$, is presumed known. This flux is attributed to automobile and smoke stack emissions. It is also known that the concentration of $\mathrm{NO}_{2}$ at a distance well above ground level is zero and that $\mathrm{NO}_{2}$ reacts chemically in the atmosphere. In particular, $\mathrm{NO}_{2}$ reacts with unburned hydrocarbons (in a process that is activated by sunlight) to produce PAN (peroxyacetylnitrate), the final product of photochemical smog. The reaction is first order, and the local rate at which it occurs may be expressed as $\dot{N}_{\mathrm{A}}=-k_{1} C_{\mathrm{A}}$.
(a) Assuming steady-state conditions and a stagnant atmosphere, obtain an expression for the vertical distribution $C_{\mathrm{A}}(x)$ of the molar concentration of $\mathrm{NO}_{2}$ in the atmosphere.
(b) If an $\mathrm{NO}_{2}$ partial pressure of $p_{\mathrm{A}}=2 \times 10^{-6}$ bar is sufficient to cause pulmonary damage, what is the value of the ground level molar flux for which you would issue a smog alert? You may assume an isothermal atmosphere at $T=300 \mathrm{~K}$, a reaction coefficient of $k_{1}=0.03 \mathrm{~s}^{-1}$, and an $\mathrm{NO}_{2}$-air diffusion coefficient of $D_{\mathrm{AB}}=0.15 \times 10^{-4} \mathrm{~m}^{2} / \mathrm{s}$.

Lottie Adams
Lottie Adams
Numerade Educator
03:37

Problem 39

In Problem $14.38, \mathrm{NO}_{2}$ transport by diffusion in a stagnant atmosphere was considered for steady-state conditions. However, the problem is actually time dependent, and a more realistic approach would account for transient effects. Consider the ground level emission of $\mathrm{NO}_{2}$ to begin in the early morning (at $t=0$ ), when the $\mathrm{NO}_{2}$ concentration in the atmosphere is everywhere zero. Emission occurs throughout the day at a constant flux $N_{\mathrm{A}, 0}^{\prime \prime}$, and the $\mathrm{NO}_{2}$ again experiences a first-order photochemical reaction in the atmosphere $\left(\dot{N}_{\mathrm{A}}=-k_{1} C_{\mathrm{A}}\right)$.
(a) For a differential element in the atmosphere, derive a differential equation that could be used to determine the molar concentration $C_{\mathrm{A}}(x, t)$. State appropriate initial and boundary conditions.
(b) Obtain an expression for $C_{\mathrm{A}}(x, t)$ under the special condition for which photochemical reactions may be neglected. For this condition what are the molar concentrations of $\mathrm{NO}_{2}$ at ground level and at $100-\mathrm{m}$ elevation $3 \mathrm{~h}$ after the start of the emissions, if $N_{\mathrm{A}, 0}^{\prime \prime}=3 \times 10^{-11} \mathrm{kmol} / \mathrm{s} \cdot \mathrm{m}^{2}$ and $D_{\mathrm{AB}}=0.15 \times 10^{-4} \mathrm{~m}^{2} / \mathrm{s} ?$

Lottie Adams
Lottie Adams
Numerade Educator
01:13

Problem 40

A large sheet of material $40 \mathrm{~mm}$ thick contains dissolved hydrogen $\left(\mathrm{H}_{2}\right)$ having a uniform concentration of $3 \mathrm{kmol} / \mathrm{m}^{3}$. The sheet is exposed to a fluid stream that causes the concentration of the dissolved hydrogen to be reduced suddenly to zero at both surfaces. This surface condition is maintained constant thereafter. If the mass diffusivity of hydrogen is $9 \times 10^{-7} \mathrm{~m}^{2} / \mathrm{s}$, how much time is required to bring the density of dissolved hydrogen to a value of $1.2 \mathrm{~kg} / \mathrm{m}^{3}$ at the center of the sheet?

Narayan Hari
Narayan Hari
Numerade Educator
03:30

Problem 41

A common procedure for increasing the moisture content of air is to bubble it through a column of water. Assume the air bubbles to be spheres of radius $r_{o}=1 \mathrm{~mm}$ and to be in thermal equilibrium with the water at $25^{\circ} \mathrm{C}$. How long should the bubbles remain in the water to achieve a vapor concentration at the center that is $99 \%$ of the maximum possible (saturated) concentration? The air is dry when it enters the water.

Surendra Kumar
Surendra Kumar
Numerade Educator
01:03

Problem 42

Consider Problem 14.41.
(a) How long should the bubbles remain in the water to achieve an average vapor concentration that is $95 \%$ of the maximum value?
(b) How long should the bubbles remain in the water to achieve an average vapor concentration that is $50 \%$ of the maximum value?

Mayukh Banik
Mayukh Banik
Numerade Educator
03:59

Problem 43

Steel is carburized in a high-temperature process that depends on the transfer of carbon by diffusion. The value of the diffusion coefficient is strongly temperature dependent and may be approximated as $D_{\mathrm{C}-\mathrm{s}}$ $\left(\mathrm{m}^{2} / \mathrm{s}\right) \approx 2 \times 10^{-5} \exp [-17,000 / T(\mathrm{~K})]$. If the process is effected at $1000^{\circ} \mathrm{C}$ and a carbon mole fraction of $0.02$ is maintained at the surface of the steel, how much time is required to elevate the carbon content of the steel from an initial value of $0.1 \%$ to a value of $1.0 \%$ at a depth of $1 \mathrm{~mm}$ ?

Narayan Hari
Narayan Hari
Numerade Educator
02:30

Problem 44

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 $t$.

Narayan Hari
Narayan Hari
Numerade Educator
08:51

Problem 45

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).

Puneet Prajapati
Puneet Prajapati
Numerade Educator
08:40

Problem 46

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?

David Collins
David Collins
Numerade Educator
18:47

Problem 47

If an amount of energy $Q_{o}^{\prime \prime}\left(\mathrm{J} / \mathrm{m}^{2}\right)$ is released instantaneously, as, for example, from a pulsed laser, and it is absorbed by the surface of a semi-infinite medium, with no attendant losses to the surroundings, the subsequent temperature distribution in the medium is
$$
T(x, t)-T_{i}=\frac{Q_{o}^{\prime \prime}}{\rho c(\pi \alpha t)^{1 / 2}} \exp \left(-x^{2} / 4 \alpha t\right)
$$
where $T_{i}$ is the initial, uniform temperature of the medium. Consider an analogous mass transfer process involving deposition of a thin layer of phosphorous (P) on a silicon (Si) wafer at room temperature. If the wafer is placed in a furnace, the diffusion of $\mathrm{P}$ into Si is significantly enhanced by the high-temperature environment.
A Si wafer with $1-\mu \mathrm{m}$-thick P film is suddenly placed in a furnace at $1000^{\circ} \mathrm{C}$, and the resulting distribution of $P$ is characterized by an expression of the form
$$
C_{\mathrm{P}}(x, t)=\frac{M_{\mathrm{P}, o}^{\prime \prime}}{\left(\pi D_{\mathrm{P}-\mathrm{Si}} t\right)^{1 / 2}} \exp \left(-x^{2} / 4 D_{\mathrm{P}-\mathrm{Si}} t\right)
$$
where $M_{\mathrm{P}, o}^{\prime \prime}$ is the molar area density $\left(\mathrm{kmol} / \mathrm{m}^{2}\right)$ of $\mathrm{P}$ associated with the film of concentration $C_{\mathrm{P}}$ and thickness $d_{o}$.
(a) Explain the correspondence between variables in the analogous temperature and concentration distributions.
(b) Determine the mole fraction of $P$ at a depth of $0.1 \mu \mathrm{m}$ in the Si after $30 \mathrm{~s}$. The diffusion coefficient is $D_{\mathrm{P}-\mathrm{Si}}=1.2 \times 10^{-17} \mathrm{~m}^{2} / \mathrm{s}$. The mass densities of $\mathrm{P}$ and $\mathrm{Si}$ are 2000 and $2300 \mathrm{~kg} / \mathrm{m}^{3}$, respectively, and their molecular weights are $30.97$ and $28.09 \mathrm{~kg} / \mathrm{kmol}$.

Niamat Khuda
Niamat Khuda
Numerade Educator
04:49

Problem 48

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 $\left(k_{1} \approx 0\right)$ ?

Shazia Naz
Shazia Naz
Numerade Educator
05:57

Problem 49

Consider a DVD similar to that of Problem 5.99. To protect sensitive information within the storage medium, a very thin film of reactive polymer is embedded within the polycarbonate at a distance $d=0.5 \mathrm{~mm}$ from the surface. The thin film can undergo a chemical reaction with oxygen during which it is converted from a transparent material to an opaque material, rendering the information unreadable. The chemical reaction begins when the oxygen concentration at the reactive polymer reaches $C_{\text {crit }}=5 \times 10^{-5} \mathrm{kmol} / \mathrm{m}^{3}$. The DVD is shipped in an oxygen-proof pouch; determine the elapsed time after removal from the pouch before the DVD selfdestructs. The solubility and diffusivity of oxygen in polycarbonate are $S=8.9 \times 10^{-3} \mathrm{kmol} / \mathrm{m}^{3}$. bar and $D_{\mathrm{AB}}=6.5 \times 10^{-12} \mathrm{~m}^{2} / \mathrm{s}$, respectively.

Dr.  Satish  Ingale
Dr. Satish Ingale
Numerade Educator
02:43

Problem 50

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.

Mohamed Raafat Mohamed
Mohamed Raafat Mohamed
Numerade Educator
19:42

Problem 51

Hydrogen gas is used in a process to manufacture a sheet material of $6-\mathrm{mm}$ thickness. At the end of the process, $\mathrm{H}_{2}$ remains in solution in the material with a uniform concentration of $320 \mathrm{kmol} / \mathrm{m}^{3}$. To remove $\mathrm{H}_{2}$ from the material, both surfaces of the sheet are exposed to an airstream at $500 \mathrm{~K}$ and a total pressure of $3 \mathrm{~atm}$. Due to contamination, the hydrogen partial pressure is $0.1 \mathrm{~atm}$ in the airstream, which provides a convection mass transfer coefficient of $1.5 \mathrm{~m} / \mathrm{h}$. The mass diffusivity and solubility of hydrogen (A) in the sheet material (B) are $D_{\mathrm{AB}}=2.6 \times 10^{-8} \mathrm{~m}^{2} / \mathrm{s}$ and $S_{\mathrm{AB}}=160 \mathrm{kmol} / \mathrm{m}^{3} \cdot$ atm, respectively.
(a) If the sheet material is left exposed to the airstream for a long time, determine the final content of hydrogen in the material $\left(\mathrm{kg} / \mathrm{m}^{3}\right)$.
(b) Identify and evaluate the parameter that can be used to determine whether the transient mass diffusion process in the sheet can be assumed to be characterized by a uniform concentration at any time during the process. Hint: This situation is analogous to that used to determine the validity of the lumped-capacitance method for a transient heat transfer analysis.
(c) Determine the time required to reduce the hydrogen mass density at the center of the sheet to twice the limiting value calculated in part (a).

Chareen Guzman
Chareen Guzman
Numerade Educator
19:42

Problem 52

Consider the hydrogen-removal process described in Problem $14.51$, but under conditions for which the mass diffusivity of the hydrogen gas (A) in the sheet material (B) is $D_{\mathrm{AB}}=1.8 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}$ (instead of $\left.2.6 \times 10^{-8} \mathrm{~m}^{2} / \mathrm{s}\right)$. With the smaller value of $D_{\mathrm{AB}}$, a uniform concentration may no longer be assumed to exist in the material during the removal process.
(a) If the sheet material is left exposed to the airstream for a very long time, what is the final content of hydrogen in the material $\left(\mathrm{kg} / \mathrm{m}^{3}\right)$ ?
(b) Identify and evaluate the parameters that describe the transient mass diffusion process in the sheet. Hint: The situation is analogous to that of transient heat conduction in a plane wall.
(c) Determine the time required to reduce the hydrogen mass density at the center of the sheet to twice the limiting value calculated in part (a).
(d) Assuming a uniform concentration at any time during the removal process, calculate the time required to reach twice the limiting density calculated in part (a). Compare the result with that obtained from part (c), and explain the differences.

Chareen Guzman
Chareen Guzman
Numerade Educator
18:30

Problem 53

A 1-mm-thick square $(100 \mathrm{~mm} \times 100 \mathrm{~mm})$ sheet of polymer is suspended from a precision scale in a chamber characterized by a temperature and relative humidity of $T=300 \mathrm{~K}$ and $\phi=0$, respectively. Suddenly, at time $t=0$, the chamber's relative humidity is raised to $\phi=0.95$. The measured mass of the sheet increases by $0.012 \mathrm{mg}$ over $24 \mathrm{~h}$ and by $0.016 \mathrm{mg}$ over $48 \mathrm{~h}$. Determine the solubility and mass diffusivity of water vapor in the polymer. Preliminary experiments have indicated that the mass diffusivity is greater than $7 \times 10^{-13} \mathrm{~m}^{2} / \mathrm{s}$.

Susan Hallstrom
Susan Hallstrom
Numerade Educator
02:02

Problem 54

14.54 A vitreous silica optical fiber of diameter $100 \mu \mathrm{m}$ is used to send optical signals from a sensor placed deep inside a hydrogen chamber. The hydrogen is at a pressure of 20 bars. The mass diffusivity and solubility of the hydrogen in the glass fiber are $D_{\mathrm{AB}}=2.88 \times 10^{-15}$ $\mathrm{m}^{2} / \mathrm{s}$ and $S=4.15 \times 10^{-3} \mathrm{kmol} / \mathrm{m}^{3}$ - bar, respectively. Hydrogen diffusion into the fiber is undesirable, since it changes the spectral transmissivity and refractive index of the glass and can lead to failure of the detection system.
(a) Determine the average hydrogen concentration in an uncoated optical fiber, $\bar{C}$, after $100 \mathrm{~h}$ of operation in the hydrogen environment. Determine the corresponding change in the refractive index, $\Delta n$, of the fiber. For vitreous silica, $\Delta n=\left(1.6 \times 10^{-3} \mathrm{~m}^{3} / \mathrm{kmol}\right) \times \bar{C}$.(b) Determine the average hydrogen concentration and change in refractive index after $1 \mathrm{~h}$ and $10 \mathrm{~h}$ of operation in the hydrogen environment.

Mayukh Banik
Mayukh Banik
Numerade Educator
07:06

Problem 55

The surface of glass quickly develops very small microcracks when exposed to high humidity. Although microcracks can be safely ignored in most applications, they can significantly decrease the mechanical strength of very small glass structures such as optical fibers. Consider a glass optical fiber of diameter $D_{i}=125 \mu \mathrm{m}$ that is coated with an acrylate polymer to form a coated fiber of outer diameter $D_{o}=250 \mu \mathrm{m}$.
A telecommunications engineer insists that the optical fiber be stored in a low-humidity environment prior to installation so that it is sufficiently strong to withstand rough treatment by technicians in the field. If installation of a roll of fiber requires several hot and humid days to complete, will careful storage beforehand prevent microcracking? The mass diffusivity of water vapor in the acrylate is $D_{\mathrm{AB}}=5.5 \times 10^{-13} \mathrm{~m}^{2} / \mathrm{s}$ while the glass can be considered impermeable.

Tara Appleyard
Tara Appleyard
Numerade Educator
00:57

Problem 56

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?

Manish Jain
Manish Jain
Numerade Educator