Chapter 3: Problem 60
How much error would one expect in determining the specific enthalpy by applying the incompressible-liquid approximation to water at 3000 psia and \(400^{\circ} \mathrm{F} ?\)
Chapter 3: Problem 60
How much error would one expect in determining the specific enthalpy by applying the incompressible-liquid approximation to water at 3000 psia and \(400^{\circ} \mathrm{F} ?\)
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Get started for freeWater is boiling at 1 atm pressure in a stainless steel pan on an electric range. It is observed that 2 kg of liquid water evaporates in 30 min. The rate of heat transfer to the water is \((a) 2.51 \mathrm{kW}\) (b) \(2.32 \mathrm{kW}\) \((c) 2.97 \mathrm{kW}\) \((d) 0.47 \mathrm{kW}\) \((e) 3.12 \mathrm{kW}\)
A spherical balloon with a diameter of \(9 \mathrm{m}\) is filled with helium at \(27^{\circ} \mathrm{C}\) and 200 kPa. Determine the mole number and the mass of the helium in the balloon. Answers: \(30.6 \mathrm{kmol}, 123 \mathrm{kg}.\)
A \(300-\mathrm{m}^{3}\) rigid tank is filled with saturated liquidvapor mixture of water at \(200 \mathrm{kPa}\). If 25 percent of the mass is liquid and 75 percent of the mass is vapor, the total mass in the tank is \((a) 451 \mathrm{kg}\) \((b) 556 \mathrm{kg}\) \((c) 300 \mathrm{kg}\) \((d) 331 \mathrm{kg}\) \((e) 195 \mathrm{kg}\)
Refrigerant- \(134 \mathrm{a}\) at 400 psia has a specific volume of \(0.1144 \mathrm{ft}^{3} / \mathrm{lbm} .\) Determine the temperature of the refrigerant based on \((a)\) the ideal-gas equation, \((b)\) the van der Waals equation, and ( \(c\) ) the refrigerant tables.
Water initially at 200 kPa and \(300^{\circ} \mathrm{C}\) is contained in a piston-cylinder device fitted with stops. The water is allowed to cool at constant pressure until it exists as a saturated vapor and the piston rests on the stops. Then the water continues to cool until the pressure is \(100 \mathrm{kPa}\). On the \(T\) -v diagrams sketch, with respect to the saturation lines, the process curves passing through both the initial, intermediate, and final states of the water. Label the \(T, P\) and \(v\) values for end states on the process curves. Find the overall change in internal energy between the initial and final states per unit mass of water.
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