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820 | <strong>Thermodynamics</strong>16–60C Using the Henry’s constant data for a gas dissolvedin a liquid, explain how you would determine the mole fractionof the gas dissolved in the liquid at the interface at aspecified temperature.16–61 Show that a mixture of saturated liquid water andsaturated water vapor at 100°C satisfies the criterion forphase equilibrium.16–62 Show that a mixture of saturated liquid water andsaturated water vapor at 300 kPa satisfies the criterion forphase equilibrium.16–63 Show that a saturated liquid–vapor mixture of refrigerant-134aat 10°C satisfies the criterion for phase equilibrium.16–64 Consider a mixture of oxygen and nitrogen in thegas phase. How many independent properties are needed tofix the state of the system? Answer: 316–65 In absorption refrigeration systems, a two-phaseequilibrium mixture of liquid ammonia (NH 3 ) and water(H 2 O) is frequently used. Consider a liquid–vapor mixture ofammonia and water in equilibrium at 30°C. If the compositionof the liquid phase is 60 percent NH 3 and 40 percentH 2 O by mole numbers, determine the composition of thevapor phase of this mixture. Saturation pressure of NH 3 at30°C is 1167.4 kPa.16–66 Consider a liquid–vapor mixture of ammonia andwater in equilibrium at 25°C. If the composition of the liquidphase is 50 percent NH 3 and 50 percent H 2 O by mole numbers,determine the composition of the vapor phase of thismixture. Saturation pressure of NH 3 at 25°C is 1003.5 kPa.Answers: 0.31 percent, 99.69 percent16–67 A two-phase mixture of ammonia and water is inequilibrium at 50°C. If the composition of the vapor phase is99 percent NH 3 and 1 percent H 2 O by mole numbers, determinethe composition of the liquid phase of this mixture. Saturationpressure of NH 3 at 50°C is 2033.5 kPa.16–68 Using the liquid–vapor equilibrium diagram of anoxygen–nitrogen mixture, determine the composition of eachphase at 80 K and 100 kPa.16–69 Using the liquid–vapor equilibrium diagram of anoxygen–nitrogen mixture, determine the composition of eachphase at 84 K and 100 kPa.16–70 Using the liquid–vapor equilibrium diagram of anoxygen–nitrogen mixture at 100 kPa, determine the temperatureat which the composition of the vapor phase is 79 percentN 2 and 21 percent O 2 . Answer: 82 K16–71 Using the liquid–vapor equilibrium diagram of anoxygen–nitrogen mixture at 100 kPa, determine the temperatureat which the composition of the liquid phase is 30 percentN 2 and 70 percent O 2 .16–72 Consider a rubber plate that is in contact with nitrogengas at 298 K and 250 kPa. Determine the molar and massdensity of nitrogen in the rubber at the interface.16–73 A wall made of natural rubber separates O 2 and N 2gases at 25°C and 500 kPa. Determine the molar concentrationsof O 2 and N 2 in the wall.16–74 Consider a glass of water in a room at 27°C and 97kPa. If the relative humidity in the room is 100 percent andthe water and the air are in thermal and phase equilibrium,determine (a) the mole fraction of the water vapor in the airand (b) the mole fraction of air in the water.16–75E Water is sprayed into air at 80°F and 14.3 psia, andthe falling water droplets are collected in a container on thefloor. Determine the mass and mole fractions of air dissolvedin the water.16–76 Consider a carbonated drink in a bottle at 27°C and130 kPa. Assuming the gas space above the liquid consists ofa saturated mixture of CO 2 and water vapor and treating thedrink as water, determine (a) the mole fraction of the watervapor in the CO 2 gas and (b) the mass of dissolved CO 2 in a300-ml drink.Review Problems16–77 Using the Gibbs function data, determine the equilibriumconstant K P for the dissociation process O 2∆2O at 2000 K. Compare your result with the K P value listedin Table A–28. Answer: 4.4 10 716–78 A mixture of 1 mol of H 2 and 1 mol of Ar is heatedat a constant pressure of 1 atm until 15 percent of H 2 dissociatesinto monatomic hydrogen (H). Determine the final temperatureof the mixture.16–79 A mixture of 1 mol of H 2 O, 2 mol of O 2 , and 5 mol ofN 2 is heated to 2200 K at a pressure of 5 atm. Assuming theequilibrium mixture consists of H 2 O, O 2 ,N 2 , and H 2 , determinethe equilibrium composition at this state. Is it realistic toassume that no OH will be present in the equilibrium mixture?16–80 Determine the mole fraction of argon that ionizesaccording to the reaction Ar ∆ Ar e at 10,000 Kand 0.35 atm (K P 0.00042 for this reaction).16–81 Methane gas (CH 4 ) at 25°C is burned with thestoichiometric amount of air at 25°C during anadiabatic steady-flow combustion process at 1 atm. Assumingthe product gases consist of CO 2 , H 2 O, CO, N 2 , and O 2 ,determine (a) the equilibrium composition of the productgases and (b) the exit temperature.16–82 Reconsider Prob. 16–81. Using EES (or other)software, study the effect of excess air on theequilibrium composition and the exit temperature by varyingthe percent excess air from 0 to 200 percent. Plot the exittemperature against the percent excess air, and discuss theresults.

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