Chapter 14: Problem 34
Using Henry's constant data for a gas dissolved in a liquid, explain how you would determine the mole fraction of the gas dissolved in the liquid at the interface at a specified temperature.
Chapter 14: Problem 34
Using Henry's constant data for a gas dissolved in a liquid, explain how you would determine the mole fraction of the gas dissolved in the liquid at the interface at a specified temperature.
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Get started for freeThe 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 \(9.5-\mathrm{mm}\)-thick gypsum wallboard to water vapor is $2.86 \times 10^{-9} \mathrm{~kg} / \mathrm{s} \cdot \mathrm{m}^{2} \cdot \mathrm{Pa}$.
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 \(23 \times 10^{-12} \mathrm{~kg} / \mathrm{s}\) - $\mathrm{m}^{2} \cdot \mathrm{Pa}$. 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.
Benzene-free air at \(25^{\circ} \mathrm{C}\) and \(101.3 \mathrm{kPa}\) enters a \(5-\mathrm{cm}\)-diameter tube at an average velocity of $5 \mathrm{~m} / \mathrm{s}$. The inner surface of the 6-m-long tube is coated with a thin film of pure benzene at \(25^{\circ} \mathrm{C}\). The vapor pressure of benzene \(\left(\mathrm{C}_{6} \mathrm{H}_{6}\right)\) at \(25^{\circ} \mathrm{C}\) is $13 \mathrm{kPa}$, and the solubility of air in benzene is assumed to be negligible. Calculate \((a)\) the average mass transfer coefficient in \(\mathrm{m} / \mathrm{s}\), (b) the molar concentration of benzene in the outlet air, and \((c)\) the evaporation rate of benzene in $\mathrm{kg} / \mathrm{h}$.
Consider one-dimensional mass diffusion of species \(A\) through a plane wall. Does the species \(A\) content of the wall change during steady mass diffusion? How about during transient mass diffusion?
Does a mass transfer process have to involve heat transfer? Describe a process that involves both heat and mass transfer.
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