/*! 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 127 The final step of a manufacturin... [FREE SOLUTION] | 91Ó°ÊÓ

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The final step of a manufacturing process in which a protective coating is applied to the inner surface of a circular tube involves passage of dry, atmosphere air through the tube to remove a residual liquid associated with the process. Consider a coated 5-m-long tube with an inner diameter of \(50 \mathrm{~mm}\). The tube is maintained at a temperature of \(300 \mathrm{~K}\), and the residual liquid exists as a thin film whose corresponding vapor pressure is \(15 \mathrm{~mm}\) Hg. The molecular weight and diffusion coefficient of the vapor are \(\Lambda_{\alpha}=70 \mathrm{~kg} / \mathrm{kmol}\) and \(D_{A B}=10^{-5} \mathrm{~m}^{2} / \mathrm{s}\), respectively. Air enters the tube at a mean velocity of \(0.5 \mathrm{~m} / \mathrm{s}\) and a temperature of \(300 \mathrm{~K}\). (a) Estimate the partial pressure and mass density of vapor in the air exiting the tube. (b) What is the rate of liquid removal from the tube in \(\mathrm{kg} / \mathrm{s}\) ?

Short Answer

Expert verified
(a) The partial pressure of vapor in the air exiting the tube is \(P_\alpha = 2005.197 \mathrm{~Pa}\), and the mass density of vapor is \(\rho_\alpha = 0.56269 \mathrm{~kg/m^3}\). (b) The rate of liquid removal from the tube is approximately \(r = 5.525 \times 10^{-4} \mathrm{~kg/s}\).

Step by step solution

01

Calculate Partial Pressure of Vapor Exiting the Tube

The given vapor pressure of the residual liquid is \(15 \mathrm{~mm}\) Hg. Let's convert it to \(Pa\) since we will use the Ideal Gas Law later: \(P = 15 \mathrm{~mm\ Hg} \times \dfrac{101325 \mathrm{~Pa}}{760 \mathrm{~mm\ Hg}} = 2005.197 \mathrm{~Pa}\) The partial pressure of the vapor exiting the tube, \(P_\alpha\), is equal to the vapor pressure, \(P\): \(P_\alpha = P = 2005.197 \mathrm{~Pa}\)
02

Calculate Mass Density of Vapor Exiting the Tube

Now, let's calculate the mass density of the vapor in the air exiting the tube using the Ideal Gas Law: \(\rho_\alpha = \frac{P_\alpha \Lambda_\alpha}{R T}\) where \(P_\alpha = 2005.197 \mathrm{~Pa}\) (partial pressure of vapor) \(\Lambda_\alpha = 70 \mathrm{~kg/kmol}\) (molecular weight of vapor) \(R = 8314.46 \mathrm{~J/(kmol\ K)}\) (universal gas constant) \(T = 300 \mathrm{~K}\) (temperature of the tube) \(\rho_\alpha = \frac{2005.197 \mathrm{~Pa} \times 70 \mathrm{~kg/kmol}}{8314.46 \mathrm{~J/(kmol\ K)} \times 300 \mathrm{~K}} = 0.56269 \mathrm{~kg/m^3}\)
03

Calculate Flow Rate of Air Entering the Tube

Find the flow rate of air entering the tube, \(Q\). Flow rate is the product of cross-sectional area, \(A\), and air mean velocity, \(V\): \(Q = A \times V\) Cross-sectional area, $A = \dfrac{\pi d^2}{4}\) where \(d = 50 \times 10^{-3} \mathrm{~m}\) (inner diameter of the tube) \(A = \dfrac{\pi (50 \times 10^{-3} \mathrm{~m})^2}{4} = 1.9635 \times 10^{-3} \mathrm{~m^2}\) Now, let's calculate the flow rate using the air mean velocity: \(Q = 1.9635 \times 10^{-3} \mathrm{~m^2} \times 0.5 \mathrm{~m/s} = 9.8174 \times 10^{-4} \mathrm{~m^3/s}\)
04

Calculate Rate of Liquid Removal from Tube

Now we will calculate the rate of liquid removal, \(r\), from the tube by multiplying the mass density of the vapor, \(\rho_\alpha\), and the flow rate, \(Q\): \(r = \rho_\alpha \times Q\) Substituting the values from Step 2 and Step 3: \(r = 0.56269 \mathrm{~kg/m^3} \times 9.8174 \times 10^{-4} \mathrm{~m^3/s}\) \(r = 5.525 \times 10^{-4} \mathrm{~kg/s}\) So, the rate of liquid removal from the tube is approximately \(5.525 \times 10^{-4} \mathrm{~kg/s}\).

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Key Concepts

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

Partial Pressure
Understanding partial pressure is key when working with gases. In our exercise, the partial pressure of the vapor is a crucial measurement. It represents the pressure that this vapor alone would exert if it occupied the entire volume. We started with the vapor pressure, given in mm Hg, and converted it to Pascals (Pa):
  • The vapor pressure is 15 mm Hg.
  • Conversion to Pascals involves the formula: \(P = 15\, \text{mm Hg} \times \frac{101325\, \text{Pa}}{760\, \text{mm Hg}} = 2005.197\, \text{Pa}\).
  • This becomes the partial pressure of the vapor exiting the tube.
Knowing partial pressure helps predict how the vapor behaves, interacts with other gases, and contributes to the overall pressure in a system.
This is fundamental in processes like diffusion and chemical reactions.
Ideal Gas Law
The Ideal Gas Law is a powerful tool in predicting the behavior of gases under different conditions. It's defined by the equation \(PV = nRT\), where:
  • \(P\) is the pressure,
  • \(V\) is the volume,
  • \(n\) is the number of moles,
  • \(R\) is the universal gas constant,
  • \(T\) is the temperature.
In this exercise, we rearranged the formula to find the mass density \(\rho_\alpha\) of the vapor:
  • \(\rho_\alpha = \frac{P_\alpha \Lambda_\alpha}{RT}\)
  • Substituting the values, we determined the mass density to be \(0.56269\, \text{kg/m}^3\).
The Ideal Gas Law helps understand the gas behavior in various conditions, like changes in pressure or temperature, which is crucial for designing chemical processes and safety measures.
Diffusion Coefficient
The diffusion coefficient is a measure that describes how quickly molecules spread. It's used to model the rate at which substances mix, driven by concentration gradients. Here, the diffusion coefficient for the vapor is given as \(D_{AB} = 10^{-5} \text{ m}^2/\text{s}\).
  • This coefficient indicates the ease with which the vapor molecules move through the air inside the tube.
  • In practical terms, it affects how quickly the vapor mixes with air and moves through the tube.
The diffusion coefficient is essential in understanding mass transfer processes, especially in systems involving gases and liquids.
By knowing this value, engineers and scientists can model and predict how different gases will interact over time, helping in designing efficient manufacturing processes.

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Most popular questions from this chapter

Dry air at \(35^{\circ} \mathrm{C}\) and a velocity of \(10 \mathrm{~m} / \mathrm{s}\) flows over a thin-walled tube of \(20-\mathrm{mm}\) diameter and \(200-\mathrm{mm}\) length, having a fibrous coating that is water-saturated. To maintain an approximately uniform surface temperature of \(27^{\circ} \mathrm{C}\), water at a prescribed flow rate and temperature passes through the tube. (a) Considering the heat and mass transfer processes on the external surface of the tube, determine the heat rate from the tube. (b) For a flow rate of \(0.025 \mathrm{~kg} / \mathrm{s}\), determine the inlet temperature, \(T_{\mathrm{mm},}\), at which water must be supplied to the tube.

In a particular application involving fluid flow at a rate \(\dot{m}\) through a circular tube of length \(L\) and diameter \(D\), the surface heat flux is known to have a sinusoidal variation with \(x\), which is of the form \(q_{s}^{\prime \prime}(x)=q_{s, m}^{\prime \prime} \sin (\pi x / L)\). The maximum flux, \(q_{s, m}^{n}\), is a known constant, and the fluid enters the tube at a known temperature, \(T_{m, i}\) Assuming the convection coefficient to be constant, how do the mean temperature of the fluid and the surface temperature vary with \(x\) ?

Air at \(1 \mathrm{~atm}\) and \(285 \mathrm{~K}\) enters a 2 -m-long rectangular duct with cross section \(75 \mathrm{~mm} \times 150 \mathrm{~mm}\). The duct is maintained at a constant surface temperature of \(400 \mathrm{~K}\), and the air mass flow rate is \(0.10 \mathrm{~kg} / \mathrm{s}\). Determine the heat transfer rate from the duct to the air and the air outlet temperature.

Consider a horizontal, thin-walled circular tube of diameter \(D=0.025 \mathrm{~m}\) submerged in a container of \(n\) octadecane (paraffin), which is used to store thermal energy. As hot water flows through the tube, heat is transferred to the paraffin, converting it from the solid to liquid state at the phase change temperature of \(T_{z}=27.4^{\circ} \mathrm{C}\). The latent heat of fusion and density of paraffin are \(h_{\text {ff }}=244 \mathrm{~kJ} / \mathrm{kg}\) and \(\rho=770 \mathrm{~kg} / \mathrm{m}^{3}\), respectively, and thermophysical properties of the water may be taken as \(c_{p}=4.185 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}, k=0.653 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), \(\mu=467 \times 10^{-6} \mathrm{~kg} / \mathrm{s} \cdot \mathrm{m}\), and \(\operatorname{Pr}=2.99\) (a) Assuming the tube surface to have a uniform temperature corresponding to that of the phase change, determine the water outlet temperature and total heat transfer rate for a water flow rate of \(0.1 \mathrm{~kg} / \mathrm{s}\) and an inlet temperature of \(60^{\circ} \mathrm{C}\). If \(H=W=0.25 \mathrm{~m}\), how long would it take to completely liquefy the paraffin, from an initial state for which all the paraffin is solid and at \(27.4^{\circ} \mathrm{C}\) ? (b) The liquefaction process can be accelerated by increasing the flow rate of the water. Compute and plot the heat rate and outlet temperature as a function of flow rate for \(0.1 \leq \dot{m} \leq 0.5 \mathrm{~kg} / \mathrm{s}\). How long would it take to melt the paraffin for \(\dot{m}=0.5 \mathrm{~kg} / \mathrm{s}\) ?

The evaporator section of a heat pump is installed in a large tank of water, which is used as a heat source during the winter. As energy is extracted from the water, it begins to freeze, creating an ice/water bath at \(0^{\circ} \mathrm{C}\), which may be used for air conditioning during the summer. Consider summer cooling conditions for which air is passed through an array of copper tubes, each of inside diameter \(D=50 \mathrm{~mm}\), submerged in the bath. (a) If air enters each tube at a mean temperature of \(T_{m, i}=24^{\circ} \mathrm{C}\) and a flow rate of \(\dot{m}=0.01 \mathrm{~kg} / \mathrm{s}\), what tube length \(L\) is needed to provide an exit temperature of \(T_{m \rho}=14^{\circ} \mathrm{C}\) ? With 10 tubes passing through a tank of total volume \(V=10 \mathrm{~m}^{3}\), which initially contains \(80 \%\) ice by volume, how long would it take to completely melt the ice? The density and latent heat of fusion of ice are \(920 \mathrm{~kg} / \mathrm{m}^{3}\) and \(3.34 \times 10^{5} \mathrm{~J} / \mathrm{kg}\), respectively. (b) The air outlet temperature may be regulated by adjusting the tube mass flow rate. For the tube length determined in part (a), compute and plot \(T_{m \rho}\) as a function of \(\dot{m}\) for \(0.005 \leq \dot{m} \leq 0.05 \mathrm{~kg} / \mathrm{s}\). If the dwelling cooled by this system requires approximately \(0.05 \mathrm{~kg} / \mathrm{s}\) of air at \(16^{\circ} \mathrm{C}\), what design and operating conditions should be prescribed for the system?

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