Chapter 14: Problem 173
Using Henry's law, show that the dissolved gases in a liquid can be driven off by heating the liquid.
Chapter 14: Problem 173
Using Henry's law, show that the dissolved gases in a liquid can be driven off by heating the liquid.
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Get started for freeA water-soaked \(10-\mathrm{cm} \times 10\)-cm-square sponge is experiencing parallel dry airflow over its surface. The average convection heat transfer coefficient of dry air at \(20^{\circ} \mathrm{C}\) flowing over the sponge surface is estimated to be \(30 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), and the sponge surface is maintained at \(30^{\circ} \mathrm{C}\). If the sponge is placed under an array of radiant lamps, determine \((a)\) the rate of evaporation of water from the sponge and \((b)\) the net radiation heat transfer rate.
Does a mass transfer process have to involve heat transfer? Describe a process that involves both heat and mass transfer.
What is the low mass flux approximation in mass transfer analysis? Can the evaporation of water from a lake be treated as a low mass flux process?
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?
A glass bottle washing facility uses a well-agitated hot water bath at \(50^{\circ} \mathrm{C}\) with an open top that is placed on the ground. The bathtub is \(1 \mathrm{~m}\) high, \(2 \mathrm{~m}\) wide, and \(4 \mathrm{~m}\) long and is made of sheet metal so that the outer side surfaces are also at about \(50^{\circ} \mathrm{C}\). The bottles enter at a rate of 800 per minute at ambient temperature and leave at the water temperature. Each bottle has a mass of \(150 \mathrm{~g}\) and removes \(0.6 \mathrm{~g}\) of water as it leaves the bath wet. Makeup water is supplied at \(15^{\circ} \mathrm{C}\). If the average conditions in the plant are \(1 \mathrm{~atm}, 25^{\circ} \mathrm{C}\), and 50 percent relative humidity, and the average temperature of the surrounding surfaces is \(15^{\circ} \mathrm{C}\), determine \((a)\) the amount of heat and water removed by the bottles themselves per second, (b) the rate of heat loss from the top surface of the water bath by radiation, natural convection, and evaporation, \((c)\) the rate of heat loss from the side surfaces by natural convection and radiation, and \((d)\) the rate at which heat and water must be supplied to maintain steady operating conditions. Disregard heat loss through the bottom surface of the bath, and take the emissivities of sheet metal and water to be \(0.61\) and \(0.95\), respectively.
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