Five kg of water is contained in a piston-cylinder assembly, initially at 5 bar and 240°C. The water is slowly heated at constant pressure to a final state. The heat transfer for t... Five kg of water is contained in a piston-cylinder assembly, initially at 5 bar and 240°C. The water is slowly heated at constant pressure to a final state. The heat transfer for the process is 2960 kJ and kinetic and potential energy effects are negligible. Determine the final volume, in m³, and the work for the process, in kJ.

Understand the Problem
The question describes a thermodynamic process where water is heated in a piston-cylinder assembly under constant pressure. Given the initial conditions (pressure, temperature) and the heat transfer, the problem asks us to determine the final volume (V2) in m^3 and the work done during the process in kJ.
Answer
$V_2 = 3.5035 \text{ m}^3$
Answer for screen readers
$V_2 = 3.5035 \text{ m}^3$
Steps to Solve
- Find the specific enthalpy and specific volume at the initial state
Given $P_1 = 5 \text{ bar} = 0.5 \text{ MPa}$ and $T_1 = 240^\circ\text{C}$, we can find the specific enthalpy $h_1$ and specific volume $v_1$ from the steam tables. At this state, water is superheated vapor so we look at the superheated steam tables.
$h_1 = 2939.9 \text{ kJ/kg}$ $v_1 = 0.46462 \text{ m}^3\text{/kg}$
- Apply the first law of thermodynamics to find the specific enthalpy at the final state
Since kinetic and potential energy effects are negligible, the first law of thermodynamics for a constant pressure process simplifies to:
$Q = m(h_2 - h_1)$
Where: $Q$ is the heat transfer = 2960 kJ $m$ is the mass = 5 kg $h_1$ is the initial specific enthaply $h_2$ is the final specific enthaply
Solving for $h_2$: $h_2 = \frac{Q}{m} + h_1$ $h_2 = \frac{2960 \text{ kJ}}{5 \text{ kg}} + 2939.9 \text{ kJ/kg} = 592 \text{ kJ/kg} + 2939.9 \text{ kJ/kg} = 3531.9 \text{ kJ/kg}$
- Find the specific volume at the final state
Since the pressure is constant, $P_2 = P_1 = 5 \text{ bar} = 0.5 \text{ MPa}$. We have $P_2 = 0.5 \text{ MPa}$ and $h_2 = 3531.9 \text{ kJ/kg}$. Using the superheated steam tables again, we find the specific volume $v_2$ at this state. By interpolation:
At 0.5 MPa: h = 3484.5 kJ/kg, v = 0.6821 m^3/kg h = 3635.6 kJ/kg, v = 0.7415 m^3/kg
$v_2 = 0.6821 + \frac{3531.9-3484.5}{3635.6-3484.5}(0.7415-0.6821) = 0.6821 + \frac{47.4}{151.1}(0.0594) = 0.6821+0.0186 = 0.7007 \text{ m}^3\text{/kg}$
- Calculate the final volume
The final volume $V_2$ is given by: $V_2 = m \cdot v_2 = 5 \text{ kg} \cdot 0.7007 \text{ m}^3\text{/kg} = 3.5035 \text{ m}^3$
$V_2 = 3.5035 \text{ m}^3$
More Information
The process is an isobaric (constant pressure) heating of water, causing it to expand from one superheated state to another.
Tips
A common mistake is failing to recognize that the water is in the superheated region and using saturated water tables instead. Also, interpolation errors when looking up values in steam tables can occur.
AI-generated content may contain errors. Please verify critical information