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\(0.75-\mathrm{kg}\) water that is initially at \(0.5 \mathrm{MPa}\) and 30 percent quality occupies a spring-loaded piston-cylinder device. This device is now cooled until the water is a saturated liquid at \(100^{\circ} \mathrm{C}\). Calculate the total work produced during this process, in \(\mathrm{kJ}\).

Short Answer

Expert verified
Answer: The total work produced during the process is 501.975 kJ.

Step by step solution

01

Determine the initial and final state properties

First, we must identify all given properties of the initial and final states. Initial State: - Mass (m) = 0.75 kg - Pressure (P1) = 0.5 MPa = 500 kPa - Quality (x) = 30% = 0.3 We will need to use the steam tables to find the values of the initial specific volume (v1) and specific internal energy (u1). Final State: - Temperature (T2) = 100 °C - Saturated liquid We will also use the steam tables to find the values of the final specific volume (v2) and specific internal energy (u2).
02

Calculate initial specific volume (v1) and specific internal energy (u1)

Using the Pressure (P1 = 500 kPa) and the Quality (x = 0.3), we can determine the initial specific volume (v1) and specific internal energy (u1) from the steam table. The equations are: v1 = vf + x * (vg - vf) u1 = uf + x * (ug - uf) where vf and vg are the specific volumes of the saturated liquid and saturated vapor at the given pressure, and uf and ug are the specific internal energies of the saturated liquid and saturated vapor at the given pressure. From the steam table: For 500 kPa: - vf = 0.001053 m³/kg - vg = 0.3741 m³/kg - uf = 640.23 kJ/kg - ug = 2100.8 kJ/kg Now, we can calculate v1 and u1: v1 = 0.001053 + 0.3 * (0.3741 - 0.001053) = 0.1133681 m³/kg u1 = 640.23 + 0.3 * (2100.8 - 640.23) = 1086.4 kJ/kg
03

Calculate final specific volume (v2) and specific internal energy (u2) at 100 °C

Since the final state is a saturated liquid at 100 °C, we can directly obtain the values of v2 (vf at 100 °C), and u2 (uf at 100°C) from the steam table. From the steam table: For 100 °C: - vf = 0.001044 m³/kg - uf = 419.1 kJ/kg Hence, v2 = 0.001044 m³/kg u2 = 419.1 kJ/kg
04

Calculate the work produced during the process

We will use the first law of thermodynamics as follows: W = m * (u1 - u2) - m * P1 * (v1 - v2) Here, m is the mass of the water, and P1 is the initial pressure. Using our values: W = 0.75 * (1086.4 - 419.1) - 0.75 * 500 * (0.1133681 - 0.001044) = 501.975 kJ
05

Report the result

The total work produced during the process is 501.975 kJ.

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Most popular questions from this chapter

A mass of \(1.5 \mathrm{kg}\) of air at \(120 \mathrm{kPa}\) and \(24^{\circ} \mathrm{C}\) is contained in a gas-tight, frictionless piston-cylinder device. The air is now compressed to a final pressure of 600 kPa. During the process, heat is transferred from the air such that the temperature inside the cylinder remains constant. Calculate the work input during this process.

An insulated rigid tank initially contains \(1.4-\mathrm{kg}\) saturated liquid water at \(200^{\circ} \mathrm{C}\) and air. At this state, 25 percent of the volume is occupied by liquid water and the rest by air. Now an electric resistor placed in the tank is turned on, and the tank is observed to contain saturated water vapor after 20 min. Determine \((a)\) the volume of the \(\tan \mathrm{k},(b)\) the final temperature, and \((c)\) the electric power rating of the resistor. Neglect energy added to the air.

The specific heat at constant volume for an ideal gas is given by \(c_{v}=0.7+\left(2.7 \times 10^{-4}\right) T(\mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K})\) where \(T\) is in kelvin. The change in the internal energy for this ideal gas undergoing a process in which the temperature changes from 27 to \(127^{\circ} \mathrm{C}\) is most nearly \((a) 70 \mathrm{kJ} / \mathrm{kg}\) \((b) 72.1 \mathrm{kJ} / \mathrm{kg}\) \((c) 79.5 \mathrm{kJ} / \mathrm{kg}\) \((d) 82.1 \mathrm{kJ} / \mathrm{kg}\) \((e) 84.0 \mathrm{kJ} / \mathrm{kg}\)

Hydrogen is contained in a piston-cylinder device at 14.7 psia and \(15 \mathrm{ft}^{3} .\) At this state, a linear spring \((F \propto x)\) with a spring constant of \(15,000 \mathrm{lbf} / \mathrm{ft}\) is touching the piston but exerts no force on it. The cross-sectional area of the piston is \(3 \mathrm{ft}^{2}\). Heat is transferred to the hydrogen, causing it to expand until its volume doubles. Determine ( \(a\) ) the final pressure, ( \(b\) ) the total work done by the hydrogen, and ( \(c\) ) the fraction of this work done against the spring. Also, show the process on a \(P\) -V diagram.

Determine the enthalpy change \(\Delta h\) of nitrogen, in \(\mathrm{kJ} / \mathrm{kg}\) as it is heated from 600 to \(1000 \mathrm{K},\) using \((a)\) the empirical specific heat equation as a function of temperature (Table \(A-2 c)\) (b) the \(c_{p}\) value at the average temperature (Table \(A-2 b\) ), and \(\left.(c) \text { the } c_{p} \text { value at room temperature (Table } A-2 a\right)\).

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