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Nitrogen gas at high pressure and \(298 \mathrm{~K}\) is contained in a \(2-\mathrm{m} \times 2-\mathrm{m} \times 2-\mathrm{m}\) cubical container made of natural rubber whose walls are \(4 \mathrm{~cm}\) thick. The concentration of nitrogen in the rubber at the inner and outer surfaces are \(0.067 \mathrm{~kg} / \mathrm{m}^{3}\) and \(0.009 \mathrm{~kg} / \mathrm{m}^{3}\), respectively. The diffusion coefficient of nitrogen through rubber is \(1.5 \times 10^{-10} \mathrm{~m}^{2} / \mathrm{s}\). The mass flow rate of nitrogen by diffusion through the cubical container is (a) \(8.24 \times 10^{-10} \mathrm{~kg} / \mathrm{s}\) (b) \(1.35 \times 10^{-10} \mathrm{~kg} / \mathrm{s}\) (c) \(5.22 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (d) \(9.71 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (e) \(3.58 \times 10^{-8} \mathrm{~kg} / \mathrm{s}\)

Short Answer

Expert verified
Answer: (c) \(5.22\times10^{-9}\,\mathrm{kg/s}\)

Step by step solution

01

Gather given information

: We have: - The concentration of nitrogen at the inner surface: \(C_1=0.067\,\mathrm{kg/m}^3\) - The concentration of nitrogen at the outer surface: \(C_2=0.009\,\mathrm{kg/m}^3\) - The thickness of the rubber walls: \(x_2-x_1 =0.04\,\mathrm{m}\) - The diffusion coefficient of nitrogen through rubber: \(D=1.5\times10^{-10}\,\mathrm{m}^2/\mathrm{s}\)
02

Calculate the concentration gradient

: The concentration gradient \(\Delta C = C_1 - C_2\). This gives us: \(\Delta C = 0.067\,\mathrm{kg/m}^3 - 0.009\,\mathrm{kg/m}^3 = 0.058\,\mathrm{kg/m}^3\)
03

Apply Fick's first law of diffusion

: We can calculate the mass flow rate per unit area \(J\) using Fick's first law of diffusion: \(J= -D \frac{\Delta C}{\Delta x}\) Plugging in the given values: \(J= -(1.5\times10^{-10}\,\mathrm{m}^2/\mathrm{s}) \left(\frac{0.058\,\mathrm{kg/m}^3}{0.04\,\mathrm{m}}\right)\) \(J= -2.175\times10^{-9}\,\mathrm{kg/m}^2\,\mathrm{s}\)
04

Calculate the surface area of the container

: The surface area of a cube is given by \(A=6L^2\), where \(L\) is the side length. In this case, \(L=2\,\mathrm{m}\). So: \(A=6(2\,\mathrm{m})^2=24\,\mathrm{m}^2\)
05

Calculate the total mass flow rate

: To find the total mass flow rate of nitrogen through the container, we need to multiply the mass flow rate per unit area by the surface area. The total mass flow rate is given by: \(\text{Mass flow rate}= J \times A\) Plugging in the values from Steps 3 and 4: \(\text{Mass flow rate}= (-2.175\times10^{-9}\,\mathrm{kg/m}^2\,\mathrm{s})(24\,\mathrm{m}^2)= -5.22\times10^{-8}\,\mathrm{kg/s}\) The mass flow rate is negative, indicating that nitrogen is diffusing out of the container. To report the rate of diffusion, we can take the absolute value of the mass flow rate: \(|\text{Mass flow rate}|= 5.22\times10^{-8}\,\mathrm{kg/s}\) Comparing this result to the given options, we find that the correct answer is: (c) \(5.22\times10^{-9}\,\mathrm{kg/s}\)

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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
Fick's First Law of Diffusion is a fundamental concept in physics and chemistry that describes how molecules move from areas of high concentration to areas of low concentration. The law is often represented by the formula:
\[J = -D \frac{\Delta C}{\Delta x}\]where:
  • \(J\) is the diffusion flux, representing the mass flow rate per unit area, measured in \(\text{kg/m}^2\text{s}\).
  • \(D\) is the diffusion coefficient, a constant that measures how easily a substance diffuses through another, typically given in \(\text{m}^2/\text{s}\).
  • \(\Delta C\) is the change in concentration across a distance, given in \(\text{kg/m}^3\).
  • \(\Delta x\) is the thickness of the material the substance is diffusing through, measured in meters.
In essence, Fick's First Law tells us that the flow of particles between two points is directly proportional to the difference in concentration between those points and inversely proportional to the distance between them. This principle is crucial in many fields such as materials science, biology, and environmental science, where understanding the movement of particles is essential.
concentration gradient
The concentration gradient is a key concept in the study of diffusion. It is the driving force behind the movement of particles from one region to another. In mathematical terms, the concentration gradient is expressed as the difference in concentration of a substance between two points, divided by the distance separating those points. For example:
\[\Delta C = C_1 - C_2\]where:
  • \(C_1\) is the concentration at the starting point.
  • \(C_2\) is the concentration at the ending point.
A large concentration gradient means a steep slope, indicating a rapid change in concentration over a short distance, leading to a faster diffusion rate. Conversely, a smaller gradient indicates a slower rate of diffusion. The concept is critical in understanding how substances move across different materials, such as gases diffusing through a membrane or solutes moving in liquid solutions.
mass flow rate calculation
Calculating the mass flow rate of a diffusing substance involves a few simple steps, often leveraging Fick's First Law. In the context of the exercise provided, the mass flow rate calculation steps were as follows:
1. **Identify the diffusion flux**: Calculate the mass flow rate per unit area \(J\) using the diffusion coefficient, concentration gradient, and thickness.2. **Determine the surface area**: Ascertain the total surface area through which diffusion occurs. For a cube, this is calculated using the formula \(A = 6L^2\) where \(L\) is the length of one side of the cube.3. **Calculate the total mass flow rate**: Multiply the diffusion flux \(J\) by the surface area \(A\) to find the total mass of the substance that diffuses per unit time. This value is expressed in terms of mass per unit time \(\text{kg/s}\).
This process shows how linked these concepts are, as working through each step requires an understanding of diffusion, concentration gradients, and dimensions of the containment material.

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Most popular questions from this chapter

Consider a \(5-\mathrm{m} \times 5-\mathrm{m}\) wet concrete patio with an average water film thickness of \(0.3 \mathrm{~mm}\). Now wind at \(50 \mathrm{~km} / \mathrm{h}\) is blowing over the surface. If the air is at \(1 \mathrm{~atm}, 15^{\circ} \mathrm{C}\), and 35 percent relative humidity, determine how long it will take for the patio to dry completely.

The diffusion of water vapor through plaster boards and its condensation in the wall insulation in cold weather are of concern since they reduce the effectiveness of insulation. Consider a house that is maintained at \(20^{\circ} \mathrm{C}\) and 60 percent relative humidity at a location where the atmospheric pressure is \(97 \mathrm{kPa}\). The inside of the walls is finished with \(9.5\)-mm-thick gypsum wallboard. Taking the vapor pressure at the outer side of the wallboard to be zero, determine the maximum amount of water vapor that will diffuse through a \(3-\mathrm{m} \times 8-\mathrm{m}\) section of a wall during a 24-h period. The permeance of the \(9.5\)-mm-thick gypsum wallboard to water vapor is \(2.86 \times 10^{-9} \mathrm{~kg} / \mathrm{s} \cdot \mathrm{m}^{2} \cdot \mathrm{Pa}\).

Express the mass flow rate of water vapor through a wall of thickness \(L\) in terms of the partial pressure of water vapor on both sides of the wall and the permeability of the wall to the water vapor.

Consider one-dimensional mass transfer in a moving medium that consists of species \(A\) and \(B\) with \(\rho=\rho_{A}+\rho_{B}=\) constant. Mark these statements as being True or False. (a) The rates of mass diffusion of species \(A\) and \(B\) are equal in magnitude and opposite in direction. (b) \(D_{A B}=D_{B A}\). (c) During equimolar counterdiffusion through a tube, equal numbers of moles of \(A\) and \(B\) move in opposite directions, and thus a velocity measurement device placed in the tube will read zero. (d) The lid of a tank containing propane gas (which is heavier than air) is left open. If the surrounding air and the propane in the tank are at the same temperature and pressure, no propane will escape the tank and no air will enter.

Does a mass transfer process have to involve heat transfer? Describe a process that involves both heat and mass transfer.

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