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Water vapor at \(4.0 \mathrm{MPa}\) and \(400^{\circ} \mathrm{C}\) enters an insulated turbine operating at steady state and expands to saturated vapor at \(0.1 \mathrm{MPa}\). The effects of motion and gravity can be neglected. Determine the work developed and the exergy destruction, each in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of water vapor passing through the turbine. Let \(T_{0}=27^{\circ} \mathrm{C}, p_{0}=0.1 \mathrm{MPa}\).

Short Answer

Expert verified
The work developed is \( w_t = h_1 - h_2 \) in \( \text{kJ/kg} \), and the exergy destruction is \( e_d = T_0 (s_2 - s_1) \) in \( \text{kJ/kg} \).

Step by step solution

01

Define the Given Data

Begin by writing down all the known values from the problem: Initial pressure, \(p_1 = 4.0 \, \text{MPa}\)Initial temperature, \(T_1 = 400 \, ^\circ \text{C}\)Final pressure, \(p_2 = 0.1 \, \text{MPa}\)Ambient temperature, \(T_0 = 27 \, ^\circ \text{C} = 300 \; \text{K}\) (converted to Kelvin)
02

Determine Properties at Initial and Final States

Using a steam table, determine the specific enthalpy (\(h\)) and specific entropy (\(s\)) at the initial and final states:At \(4.0 \, \text{MPa}\) and 400 °C, find \(h_1\) and \(s_1\).At \(0.1 \, \text{MPa}\), the water vapor exits as saturated vapor: find \(h_2\) for the saturated vapor at this pressure. Also, find \(s_2\).
03

Calculate the Work Developed

The work developed per unit mass of the vapor (\(w_t\)) is the difference in enthalpy between the initial and final states: \[ w_t = h_1 - h_2 \]
04

Determine the Exergy Destruction

The exergy destruction (\(e_d\)) can be calculated using the specific entropy values and the ambient temperature: \[ e_d = T_0 \left( s_2 - s_1 \right) \]
05

Combine Results

Combine the results from the work developed and exergy destruction steps to present your final answer as per the units required.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

steady state process
A steady state process is a scenario in which the properties within the system do not change over time. This means that any mass or energy entering the system is equal to the mass or energy leaving the system. For a turbine, this concept ensures that the flow of water vapor remains consistent throughout the operation, with no accumulation inside the turbine.
In our given exercise, considering the turbine operates at steady state implies that the mass flow rate, properties like pressure and temperature, and energy transfer remain constant over time.
Practically, this assumption simplifies calculations, as it negates the need to account for transient effects or time-dependent changes. Thus, we can focus purely on initial and final state properties for our thermodynamic analysis, such as enthalpy and entropy values.
enthalpy
Enthalpy is a measure of the total heat content of a system and is symbolized as 'h'. It combines the internal energy of the system with the product of its pressure and volume.
Mathematically, it is expressed as:
h = u + pv where:
- 'u' is the internal energy
- 'p' is the pressure - 'v' is the specific volume In the turbine exercise, we use enthalpy to determine the work produced by the turbine.
By finding the specific enthalpies at the initial and final states from steam tables:
- At the initial state: h_1 - At the final state after expansion: h_2 The work developed per kilogram of water vapor passing through the turbine is the difference between these enthalpy values:
w_t = h_1 - h_2
entropy
Entropy is a measure of disorder in a system, symbolized as 's'. It indicates the dispersal of energy and provides insights into the irreversibilities within a process.
In a turbine, the entropy change between the initial and final states can be used to assess the exergy destruction.
By using steam tables, we find the specific entropy values:
- At the initial state: s_1 - At the final state after expansion: s_2 Since the process involves the turbine functioning at steady state and expanding to saturated vapor, any deviation between these entropy values signifies irreversibilities and losses. Considering the ambient temperature (T_0) or the dead state temperature, the exergy destruction is calculated using:
e_d = T_0 (s_2 - s_1). This provides a measure of the energy unaccounted for due to inefficiencies and yielded as lost work potential.
exergy
Exergy represents the maximum useful work that can be extracted from a system as it comes into equilibrium with its surroundings. Unlike energy, exergy considers the quality and potential usability. The exergy destruction in a system is a critical metric in determining inefficiencies. As discussed in the exercise, the exergy destruction is calculated through the entropy change in the system:
e_d = T_0 (s_2 - s_1) This calculation incorporates the ambient temperature (T_0), reflecting the system's loss to the environment. By analyzing the exergy destruction, we determine how much work potential is lost, guiding improvements in efficiency.
For the turbine scenario, minimizing exergy destruction is crucial for optimizing turbine performance and enhancing energy conversion efficiency.

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Most popular questions from this chapter

\(7.92\) Carbon dioxide \(\left(\mathrm{CO}_{2}\right)\) gas enters a turbine operating at steady state at 50 bar, \(500 \mathrm{~K}\) with a velocity of \(50 \mathrm{~m} / \mathrm{s}\). The inlet area is \(0.02 \mathrm{~m}^{2}\). At the exit, the pressure is 20 bar, the temperature is \(440 \mathrm{~K}\), and the velocity is \(10 \mathrm{~m} / \mathrm{s}\) The power developed by the turbine is \(3 \mathrm{MW}\), and heat transfer occurs across a portion of the surface where the average temperature is \(462 \mathrm{~K}\). Assume ideal gas behavior for the carbon dioxide and neglect the effect of gravity. Let \(T_{0}=298 \mathrm{~K}, p_{0}=1\) bar. (a) Determine the rate of heat transfer, in \(\mathrm{kW}\). (b) Perform a full exergy accounting, in \(\mathrm{kW}\), based on the net rate exergy is carried into the turbine by the carbon dioxide.

Water at \(24^{\circ} \mathrm{C}, 1\) bar is drawn from a reservoir \(1.25 \mathrm{~km}\) above a valley and allowed to flow through a hydraulic turbine- generator into a lake on the valley floor. For operation at steady state, determine the maximum theoretical rate at which electricity is generated, in MW, for a mass flow rate of \(110 \mathrm{~kg} / \mathrm{s}\). Let \(T_{0}=24^{\circ} \mathrm{C}, p_{0}=1\) bar and ignore the effects of motion.

Carbon monoxide \((\mathrm{CO})\) enters an insulated compressor operating at steady state at 10 bar, \(227^{\circ} \mathrm{C}\), and a mass flow rate of \(0.1 \mathrm{~kg} / \mathrm{s}\) and exits at 15 bar, \(327^{\circ} \mathrm{C}\). Determine the power required by the compressor and the rate of exergy destruction, each in \(\mathrm{kW}\). Ignore the effects of motion and gravity. Let \(T_{0}=17^{\circ} \mathrm{C}, p_{0}=1\) bar.

An electric water heater having a \(200-L\) capacity heats water from 23 to \(55^{\circ} \mathrm{C}\). Heat transfer from the outside of the water heater is negligible, and the states of the electrical heating element and the tank holding the water do not change significantly. Perform a full exergy accounting, in kJ, of the electricity supplied to the water heater. Model the water as incompressible with a specific heat \(c=4.18 \mathrm{~kJ} / \mathrm{kg}+\mathrm{K}\). Let \(T_{0}=23^{\circ} \mathrm{C}\).

A pump operating at steady state takes in saturated liquid water at \(65 \mathrm{lbf} / \mathrm{in}^{2}\) at a rate of \(10 \mathrm{lb} / \mathrm{s}\) and discharges water at \(1000 \mathrm{lbf} / \mathrm{in}^{2}\). The isentropic pump efficiency is \(80.22 \%\). Heat transfer with the surroundings and the effects of motion and gravity can be neglected. If \(T_{0}=75^{\circ} \mathrm{F}\), determine for the pump (a) the exergy destruction rate, in Btu/s (b) the exergetic efficiency.

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