Chapter 14: Problem 35
Using properties of saturated water, explain how you would determine the mole fraction of water vapor at the surface of a lake when the temperature of the lake surface and the atmospheric pressure are specified.
Chapter 14: Problem 35
Using properties of saturated water, explain how you would determine the mole fraction of water vapor at the surface of a lake when the temperature of the lake surface and the atmospheric pressure are specified.
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Get started for freeAir at \(52^{\circ} \mathrm{C}, 101.3 \mathrm{kPa}\), and 20 percent relative humidity enters a \(5-\mathrm{cm}\)-diameter tube with an average velocity of $6 \mathrm{~m} / \mathrm{s}$. The tube inner surface is wetted uniformly with water, whose vapor pressure at \(52^{\circ} \mathrm{C}\) is \(13.6 \mathrm{kPa}\). While the temperature and pressure of air remain constant, the partial pressure of vapor in the outlet air is increased to \(10 \mathrm{kPa}\). Detemine \((a)\) the average mass transfer coefficient in $\mathrm{m} / \mathrm{s}\(, \)(b)$ the log-mean driving force for mass transfer in molar concentration units, \((c)\) the water evaporation rate in $\mathrm{kg} / \mathrm{h}\(, and \)(d)$ the length of the tube.
A pond with an initial oxygen content of zero is to be oxygenated by forming a tent over the water surface and filling the tent with oxygen gas at \(25^{\circ} \mathrm{C}\) and \(110 \mathrm{kPa}\). Determine the mole fraction of oxygen at a depth of \(0.8 \mathrm{~cm}\) from the surface after $24 \mathrm{~h}$.
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 \(3 \mathrm{~cm}\) 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) $8.1 \times 10^{-10} \mathrm{~kg} / \mathrm{s}$ (b) \(3.2 \times 10^{-10} \mathrm{~kg} / \mathrm{s}\) (c) \(3.8 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (d) \(7.0 \times 10^{-9} \mathrm{~kg} / \mathrm{s}\) (e) \(1.60 \times 10^{-8} \mathrm{~kg} / \mathrm{s}\)
Why are the insulations on the chilled water lines always wrapped with vapor barrier jackets?
In natural convection mass transfer, the Grashof number is evaluated using density difference instead of temperature difference. Can the Grashof number evaluated this way be used in heat transfer calculations also?
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