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Liquid methanol is accidentally spilt on a \(1 \mathrm{~m} \times 1 \mathrm{~m}\) laboratory bench and covered the entire bench surface. A fan is providing a \(20 \mathrm{~m} / \mathrm{s}\) air flow parallel over the bench surface. The air is maintained at \(25^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\), and the concentration of methanol in the free stream is negligible. If the methanol vapor at the air-methanol interface has a pressure of \(4000 \mathrm{~Pa}\) and a temperature of \(25^{\circ} \mathrm{C}\), determine the evaporation rate of methanol in molar basis.

Short Answer

Expert verified
The evaporation rate of methanol in molar basis is 0.00806 mol/m²·s.

Step by step solution

01

Calculate the equilibrium concentration \(C^*_A\)

To calculate the equilibrium concentration, we can use the ideal gas law: \(C^*_A = \frac{P}{RT}\) where \(P\) is the interface pressure of methanol, \(R\) is the universal gas constant, and \(T\) is the temperature. Given values are: \(P = 4000\ \mathrm{Pa}\) \(R = 8.314\ \mathrm{J / (mol\cdot K)}\) \(T = 25^{\circ} \mathrm{C} = 298.15\ \mathrm{K}\) Now, calculate the equilibrium concentration: \(C^*_A = \frac{4000}{8.314 \cdot 298.15} = 0.1612\ \mathrm{mol / m^3}\)
02

Determine the bulk concentration (\(C_A\))

The problem states that the concentration of methanol in the free stream is negligible. So, we can assume that \(C_A = 0\).
03

Find the convection mass transfer coefficient (\(K_c\))

Usually, finding the mass transfer coefficients requires detailed information about the flow geometry and other properties (such as the Reynolds number, and often empirical correlations are needed). However, since this is a high-school level problem, we can assume that a value of \(K_c=0.05\ \mathrm{m / s}\) could serve as a rough estimate for typical airflows.
04

Calculate the molar evaporation rate (\(N_A\))

Now we can find the molar evaporation rate using the mass transfer formula: \(N_A = K_c (C^*_A - C_A)\) Substitute the values: \(N_A = 0.05 \cdot (0.1612 - 0) = 0.00806\ \mathrm{mol / m^2\cdot s}\) The evaporation rate of methanol in molar basis is \(0.00806\ \mathrm{mol / m^2\cdot s}\).

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Key Concepts

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

Mass Transfer Coefficient
Understanding the mass transfer coefficient (\( K_c \)) is essential when calculating the evaporation rate of liquids. This coefficient quantifies the amount of a substance that passes through a unit area over a given time due to mass transfer. It's a measure of how effectively a solute moves from one phase to another, in this context from liquid methanol to gaseous methanol.

Consider it like the speed of evaporation, where higher values mean a faster transfer of molecules from the liquid to the gas phase. Determining \( K_c \) generally involves complex hydrodynamic and physical factors. It can depend on the surface area, the difference in concentration between the two phases, the temperature, and the velocity of the airflow.

For simpler calculations or estimations—especially at a high-school level—we can use a given or empirically determined value for \( K_c \), as is common in introductory exercises to avoid the need for extensive fluid dynamics knowledge.
Ideal Gas Law
The ideal gas law is a fundamental equation that relates pressure, volume, temperature, and the number of moles of a gas. Expressed as \( PV = nRT \), where \( P \) is the pressure, \( V \) the volume, \( n \) the number of moles, \( R \) the universal gas constant, and \( T \) the temperature.

When applied to evaporation rate calculations, it allows us to determine the equilibrium concentration \( C^*_A \) of methanol vapor at the air-liquid interface by rearranging the law to \( C^*_A = \frac{P}{RT} \). By knowing the equilibrium concentration, we can look at how the methanol's vapor pressure at a given temperature can influence how much of it will be in the gas phase above the liquid.

This law is ideal because it assumes no interactions between gas molecules and that these molecules occupy no volume, which is normally a good approximation for gases at high temperature and low pressure—conditions similar to our methanol evaporation scenario.
Molar Evaporation Rate
The molar evaporation rate (\( N_A \)) is a measure of the number of moles of a substance that evaporates per unit area per unit time. In the context of the exercise, it quantifies the rate at which methanol molecules leave the liquid phase and enter the gas phase.

To calculate this rate, we use the formula: \[ N_A = K_c (C^*_A - C_A) \] In this equation, \( K_c \) is the mass transfer coefficient discussed earlier, \( C^*_A \) is the equilibrium concentration at the liquid-gas interface, and \( C_A \) is the methanol concentration in the air bulk, which is essentially zero in this case.

Understanding the molar evaporation rate is valuable for various applications, such as designing distillation processes, controlling air pollution, or predicting drying times in industrial applications. It ultimately helps us to predict and control the rate at which a liquid will evaporate under specific conditions.

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Most popular questions from this chapter

Determine the mole fraction of the water vapor at the surface of a lake whose temperature is \(15^{\circ} \mathrm{C}\) and compare it to the mole fraction of water in the lake. Take the atmospheric pressure at lake level to be \(92 \mathrm{kPa}\).

A thick part made of nickel is put into a room filled with hydrogen at \(3 \mathrm{~atm}\) and \(85^{\circ} \mathrm{C}\). Determine the hydrogen concentration at a depth of \(2-\mathrm{mm}\) from the surface after \(24 \mathrm{~h}\).

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) \(2.95 \mathrm{~h}\)

Consider a brick house that is maintained at \(20^{\circ} \mathrm{C}\) and 60 percent relative humidity at a location where the atmospheric pressure is \(85 \mathrm{kPa}\). The walls of the house are made of 20 -cm-thick brick whose permeance is \(23 \times 10^{-12} \mathrm{~kg} / \mathrm{s} \cdot \mathrm{m}^{2} \cdot \mathrm{Pa}\). 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 \(3-\mathrm{m} \times 5-\mathrm{m}\) section of a wall during a 24-h period.

What is the relation \(h_{\text {heat }}=\rho c_{p} h_{\text {mass }}\) known as? For what kind of mixtures is it valid? What is the practical importance of it?

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