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Consider steady one-dimensional mass diffusion through a wall. Mark these statements as being True or False. (a) Other things being equal, the higher the density of the wall, the higher the rate of mass transfer. (b) Other things being equal, doubling the thickness of the wall will double the rate of mass transfer. (c) Other things being equal, the higher the temperature, the higher the rate of mass transfer. (d) Other things being equal, doubling the mass fraction of the diffusing species at the high concentration side will double the rate of mass transfer.

Short Answer

Expert verified
a) Other things being equal, the higher the density of the wall, the higher the rate of mass transfer. b) Other things being equal, doubling the thickness of the wall will double the rate of mass transfer. c) Other things being equal, the higher the temperature, the higher the rate of mass transfer. d) Other things being equal, doubling the mass fraction of the diffusing species at the high concentration side will double the rate of mass transfer. Answer: a) False, b) False, c) True, d) True

Step by step solution

01

(Statement a)

(Statement (a) states that, other things being equal, the higher the density of the wall, the higher the rate of mass transfer. This statement is False. The rate of mass transfer depends on the diffusion coefficient, which is not directly related to the density of the wall. Increasing the density will not directly lead to an increase in the rate of mass transfer.)
02

(Statement b)

(Statement (b) states that, other things being equal, doubling the thickness of the wall will double the rate of mass transfer. This statement is False. The rate of mass transfer through a wall is inversely proportional to its thickness, according to Fick's first law of diffusion. If the thickness of the wall is doubled, the rate of mass transfer will decrease, not increase.)
03

(Statement c)

(Statement (c) states that, other things being equal, the higher the temperature, the higher the rate of mass transfer. This statement is True. Temperature affects the diffusion coefficient, which is directly related to the rate of mass transfer. As the temperature increases, the diffusion coefficient usually increases, leading to a higher rate of mass transfer.)
04

(Statement d)

(Statement (d) states that, other things being equal, doubling the mass fraction of the diffusing species at the high concentration side will double the rate of mass transfer. This statement is True. According to Fick's first law of diffusion, the rate of mass transfer is directly proportional to the concentration difference between the two sides of the wall. If the concentration at the high-concentration side is doubled, the rate of mass transfer will also double.)

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Key Concepts

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

Fick's First Law of Diffusion
Understanding Fick's first law of diffusion is essential when studying mass transfer phenomena. This law connects the rate at which particles, such as atoms or molecules, diffuse, and the concentration gradient driving this diffusion process. It states that the rate of transfer of mass of a component across a unit area is proportional to the concentration gradient. Mathematically, the law is expressed as \begin{displaymath} J = -D \frac{dC}{dx}, \begin{displaymath} where \(J\) is the diffusion flux, which measures the amount of substance that will flow through a unit area during a unit time interval. \(D\) is the diffusion coefficient, and \(\frac{dC}{dx}\) is the concentration gradient. The negative sign indicates that diffusion occurs from regions of high concentration to regions of low concentration. This concept was reinforced in the solution to the exercise by clarifying that increasing the wall's thickness would decrease, not increase, the rate of mass transfer.

This law can be applied broadly, from predicting how quickly a sugar cube will dissolve in water to understanding how gases exchange in the lungs. In our exercise scenario, it was vital to identify that Fick's Law implies an inverse relationship between the thickness of a wall and the rate of mass transfer, leading to the conclusion that statement (b) is false.
Diffusion Coefficient
The diffusion coefficient, often symbolized by \(D\), plays a crucial role in the discussion of mass transfer. It quantifies the ease with which particles move through a medium. Factors affecting \(D\) include the nature of the diffusing substance, the medium through which diffusion occurs, and the temperature and pressure conditions. The coefficient pertains to how quickly a diffusing species such as a gas, liquid, or solute can move through a solvent or membrane.

Higher values of the diffusion coefficient mean that the substance will diffuse more rapidly. This property is intrinsically tied to temperature, which was highlighted in the exercise as statement (c) and noted true—increased temperatures result in increased diffusion coefficients and therefore elevate the rate of mass transfer. Consequently, the diffusion coefficient is not merely a fixed property but is also sensitive to environmental conditions.
Concentration Difference
The concentration difference, or gradient, is a driving force for diffusion. It is the variation in concentration of a substance across a distance. Fick's first law emphasizes that diffusion is proportional to this difference; when there's a larger difference in concentration between two areas, there's a greater flux and thus a greater rate of mass transfer. The exercise illustrated this by showing that doubling the concentration difference, according to statement (d), would double the rate of mass transfer, marking it as true.

As an example, if you have a chamber filled with a perfume on one side and pure air on the other, the perfume molecules will rapidly move towards the area with less perfume concentration, diffusing until the concentration is uniform throughout the chamber. Understanding concentration gradients is fundamental in designing processes ranging from pharmaceuticals to environmental engineering.
Temperature Effect on Mass Transfer
Temperature has a significant effect on mass transfer. This is most notably seen in its influence on the diffusion coefficient, as mentioned earlier. As temperature increases, the kinetic energy of particles also increases. This higher energy leads to more rapid movement and a greater ability to overcome resistance within the medium, which enhances the rate of diffusion. In other words, at higher temperatures, molecules are more 'agitated' and can move more freely.

This relationship is reflected in statement (c) of our exercise, which was rightly identified as true. Temperature changes can dramatically influence processes such as the mixing of substances in chemical reactions, the freshness of stored food, or cooling in electronic devices. Therefore, controlling temperature is often critical in managing mass transfer in industrial and environmental systems.

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Most popular questions from this chapter

In transient mass diffusion analysis, can we treat the diffusion of a solid into another solid of finite thickness (such as the diffusion of carbon into an ordinary steel component) as a diffusion process in a semi-infinite medium? Explain.

You probably have noticed that balloons inflated with helium gas rise in the air the first day during a party but they fall down the next day and act like ordinary balloons filled with air. This is because the helium in the balloon slowly leaks out through the wall while air leaks in by diffusion. Consider a balloon that is made of \(0.1\)-mm-thick soft rubber and has a diameter of \(15 \mathrm{~cm}\) when inflated. The pressure and temperature inside the balloon are initially \(110 \mathrm{kPa}\) and \(25^{\circ} \mathrm{C}\). The permeability of rubber to helium, oxygen, and nitrogen at \(25^{\circ} \mathrm{C}\) are \(9.4 \times 10^{-13}, 7.05 \times 10^{-13}\), and \(2.6 \times 10^{-13} \mathrm{kmol} / \mathrm{m} \cdot \mathrm{s} \cdot\) bar, respectively. Determine the initial rates of diffusion of helium, oxygen, and nitrogen through the balloon wall and the mass fraction of helium that escapes the balloon during the first \(5 \mathrm{~h}\) assuming the helium pressure inside the balloon remains nearly constant. Assume air to be 21 percent oxygen and 79 percent nitrogen by mole numbers and take the room conditions to be \(100 \mathrm{kPa}\) and \(25^{\circ} \mathrm{C}\).

Define the penetration depth for mass transfer, and explain how it can be determined at a specified time when the diffusion coefficient is known.

Consider a 30-cm-diameter pan filled with water at \(15^{\circ} \mathrm{C}\) in a room at \(20^{\circ} \mathrm{C}, 1 \mathrm{~atm}\), and 30 percent relative humidity. Determine \((a)\) the rate of heat transfer by convection, (b) the rate of evaporation of water, and \((c)\) the rate of heat transfer to the water needed to maintain its temperature at \(15^{\circ} \mathrm{C}\). Disregard any radiation effects.

A glass bottle washing facility uses a well agi(Es) tated hot water bath at \(50^{\circ} \mathrm{C}\) with an open top that is placed on the ground. The bathtub is \(1 \mathrm{~m}\) high, \(2 \mathrm{~m}\) wide, and \(4 \mathrm{~m}\) long and is made of sheet metal so that the outer side surfaces are also at about \(50^{\circ} \mathrm{C}\). The bottles enter at a rate of 800 per minute at ambient temperature and leave at the water temperature. Each bottle has a mass of \(150 \mathrm{~g}\) and removes \(0.6 \mathrm{~g}\) of water as it leaves the bath wet. Makeup water is supplied at \(15^{\circ} \mathrm{C}\). If the average conditions in the plant are \(1 \mathrm{~atm}, 25^{\circ} \mathrm{C}\), and 50 percent relative humidity, and the average temperature of the surrounding surfaces is \(15^{\circ} \mathrm{C}\), determine (a) the amount of heat and water removed by the bottles themselves per second, \((b)\) the rate of heat loss from the top surface of the water bath by radiation, natural convection, and evaporation, \((c)\) the rate of heat loss from the side surfaces by natural convection and radiation, and \((d)\) the rate at which heat and water must be supplied to maintain steady operating conditions. Disregard heat loss through the bottom surface of the bath and take the emissivities of sheet metal and water to be \(0.61\) and \(0.95\), respectively.

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