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What is the difference between mass-average velocity and mole-average velocity during mass transfer in a moving medium? If one of these velocities is zero, will the other also necessarily be zero? Under what conditions will these two velocities be the same for a binary mixture?

Short Answer

Expert verified
In summary, mass-average velocity is the average velocity of particles based on their mass, while mole-average velocity is the average velocity of particles based on their number of moles. Generally, these velocities are not equal to each other and depend on the distribution of mass and moles of the individual particles in the medium. However, for a binary mixture, if the ratio of the mass of the two species is equal to the ratio of the number of moles of the two species, then both velocities will be equal. If one of these velocities is zero, the other may or may not be zero, depending on the distribution of particles' velocities.

Step by step solution

01

Definition of Mass-Average Velocity

Mass-average velocity is the average velocity of all the particles in a moving medium based on their mass. It is the ratio of the total momentum in the medium to the total mass of the medium. Mathematically speaking, mass-average velocity, \(V_{mass}\), can be expressed as follows: \(V_{mass} = \frac{\sum{m_i v_i}}{\sum{m_i}}\) Where \(m_i\) represents the mass of individual particles, and \(v_i\) represents the velocity of individual particles.
02

Definition of Mole-Average Velocity

Mole-average velocity, on the other hand, is the average velocity of all the particles in a moving medium based on their number of moles. It is the ratio of the total number of each species in the medium to the total number of all the species. Mathematically speaking, mole-average velocity, \(V_{mole}\), can be expressed as follows: \(V_{mole} = \frac{\sum{n_i v_i}}{\sum{n_i}}\) Where \(n_i\) represents the number of moles of individual particles, and \(v_i\) represents the velocity of individual particles.
03

Relationship between Mass-Average Velocity and Mole-Average Velocity

In general, mass-average velocity and mole-average velocity are not equal to each other. They depend on the distribution of mass and the number of moles of the individual particles in the medium. However, if one of these velocities is zero, the other may or may not be zero. It depends on the distribution of the particles' velocities.
04

Conditions for Mass-Average Velocity and Mole-Average Velocity to be the Same

For a binary mixture, the mass-average velocity and the mole-average velocity will be the same when the following condition is satisfied: \(\frac{m_1}{m_2} = \frac{n_1}{n_2}\) This implies that the ratio of the mass of the two species is equal to the ratio of the number of moles of the two species. Under such conditions, both velocities will be equal, and the distribution of mass and moles for the individual particles in the medium will not influence their average velocities.

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Key Concepts

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

Mass-Average Velocity
When we talk about mass-average velocity, we're referring to the weighted average speed at which all particles are moving in a fluid, with the weight being their mass. It's a tool used to characterize the overall movement of a mixture. This velocity is especially useful in engineering fields, such as chemical or mechanical engineering, where understanding how different components move is crucial for designing efficient systems.

As outlined in the exercise, the mass-average velocity (\(V_{mass}\)) is calculated by dividing the total momentum of all particles (the sum of each particle's mass times its velocity) by the total mass of the medium. Simplistically put, it's like figuring out the center speed of varying weights on a spinning carousel - heavier weights (masses) have a larger influence on this 'center speed'.

Mathematically, this concept boils down to the equation:

\(V_{mass} = \frac{\sum{m_i v_i}}{\sum{m_i}}\)

Understanding this concept is pivotal for predictive analysis and optimization in processes involving flow and mass transfer. It is important to note that this description assumes an even distribution of species, and in real-world applications, factors such as turbulence or diffusion may affect the actual mass-average velocity.
Mole-Average Velocity
Moving on to the concept of mole-average velocity, it's another type of average velocity but with a distinct focus - the number of particles, rather than their mass. The importance of this average comes into play when chemical reactions or mole-specific properties are of concern.

The mole-average velocity (\(V_{mole}\)) considers the velocity of each particle in proportion to the number of moles present. As such, it helps us understand movement in terms of molecular quantity, which can differ vastly from mass-based calculations, particularly when dealing with molecules of varying sizes and masses. The calculation for mole-average velocity is represented as:

\(V_{mole} = \frac{\sum{n_i v_i}}{\sum{n_i}}\)

Picture two gases, one light and one heavy, streaming through a pipe - the mole-average velocity would give us a sense of the average speed if we were counting molecules passing by rather than weighing them. This is especially relevant in scenarios where the molar composition precisely influences the system's behavior, such as in determining reaction rates or in the diffusion of gases.
Binary Mixture Mass Transfer
Delving deeper into the realm of mass transfer, we encounter scenarios where only two components, or a binary mixture, are being considered. The principles of mass-average and mole-average velocities are foundational in understanding and predicting the mass transfer behaviors in such systems.

In the context of binary mixtures, mass transfer refers to the process by which these two species are transported due to differences in concentration, temperature, or other driving forces. Engineers and scientists must often rely on the understanding of both velocities to design and control processes like distillation, extraction, or gas absorption.

The exercise provides a succinct condition under which the mass-average velocity and mole-average velocity converge:

\(\frac{m_1}{m_2} = \frac{n_1}{n_2}\)

That is, when the mass ratio between the two components equals their molar ratio, the velocities are identical. In real-world applications, such a condition implies that every molecule carries the same 'weight' in terms of movement, irrespective of its actual mass. This can significantly simplify calculations and process designs, albeit in ideal or specifically designed conditions. In summary, investigating binary mixture mass transfer with an understanding of these velocities can lead to more effective and optimized process engineering.

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Most popular questions from this chapter

Carbon at \(1273 \mathrm{~K}\) is contained in a \(7-\mathrm{cm}\)-innerdiameter cylinder made of iron whose thickness is \(1.2 \mathrm{~mm}\). The concentration of carbon in the iron at the inner surface is \(0.5 \mathrm{~kg} / \mathrm{m}^{3}\) and the concentration of carbon in the iron at the outer surface is negligible. The diffusion coefficient of carbon through iron is \(3 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}\). The mass flow rate of carbon by diffusion through the cylinder shell per unit length of the cylinder is (a) \(2.8 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (b) \(5.4 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (c) \(8.8 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (d) \(1.6 \times 10^{-8} \mathrm{~kg} / \mathrm{s}\) (e) \(5.2 \times 10^{-8} \mathrm{~kg} / \mathrm{s}\) 14-185 The surface of an iron component is to be hardened by carbon. The diffusion coefficient of carbon in iron at \(1000^{\circ} \mathrm{C}\) is given to be \(3 \times 10^{-11} \mathrm{~m}^{2} / \mathrm{s}\). If the penetration depth of carbon in iron is desired to be \(1.0 \mathrm{~mm}\), the hardening process must take at least (a) \(1.10 \mathrm{~h}\) (b) \(1.47 \mathrm{~h}\) (c) \(1.86 \mathrm{~h}\) (d) \(2.50 \mathrm{~h}\) (e) \(2.95 \mathrm{~h}\)

What is a concentration boundary layer? How is it defined for flow over a plate?

The solubility of hydrogen gas in steel in terms of its mass fraction is given as \(w_{\mathrm{H}_{2}}=2.09 \times 10^{-4} \exp (-3950 / T) P_{\mathrm{H}_{2}}^{0.5}\) where \(P_{\mathrm{H}_{2}}\) is the partial pressure of hydrogen in bars and \(T\) is the temperature in \(\mathrm{K}\). If natural gas is transported in a 1-cm-thick, 3-m-internal-diameter steel pipe at \(500 \mathrm{kPa}\) pressure and the mole fraction of hydrogen in the natural gas is 8 percent, determine the highest rate of hydrogen loss through a 100 -m-long section of the pipe at steady conditions at a temperature of \(293 \mathrm{~K}\) if the pipe is exposed to air. Take the diffusivity of hydrogen in steel to be \(2.9 \times 10^{-13} \mathrm{~m}^{2} / \mathrm{s}\).

The mass diffusivity of ethanol \(\left(\rho=789 \mathrm{~kg} / \mathrm{m}^{3}\right.\) and \(M=46 \mathrm{~kg} / \mathrm{kmol}\) ) through air was determined in a Stefan tube. The tube has a uniform cross-sectional area of \(0.8 \mathrm{~cm}^{2}\). Initially, the ethanol surface was \(10 \mathrm{~cm}\) from the top of the tube; and after 10 hours have elapsed, the ethanol surface was \(25 \mathrm{~cm}\) from the top of the tube, which corresponds to \(0.0445 \mathrm{~cm}^{3}\) of ethanol being evaporated. The ethanol vapor pressure is \(0.0684\) atm, and the concentration of ethanol is zero at the top of the tube. If the entire process was operated at \(24^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\), determine the mass diffusivity of ethanol in air.

The basic equation describing the diffusion of one medium through another stationary medium is (a) \(j_{A}=-C D_{A B} \frac{d\left(C_{A} / C\right)}{d x}\) (b) \(j_{A}=-D_{A B} \frac{d\left(C_{A} / C\right)}{d x}\) (c) \(j_{A}=-k \frac{d\left(C_{A} / C\right)}{d x}\) (d) \(j_{A}=-k \frac{d T}{d x}\) (e) none of them

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