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Steam heated at constant pressure in a steam generator enters the first stage of a supercritical reheat cycle at \(28 \mathrm{MPa}\), \(520^{\circ} \mathrm{C}\). Steam exiting the first-stage turbine at \(6 \mathrm{MPa}\) is reheated at constant pressure to \(500^{\circ} \mathrm{C}\). Each turbine stage has an isentropic efficiency of \(78 \%\) while the pump has an isentropic efficiency of \(82 \%\). Saturated liquid exits the condenser that operates at constant pressure, \(p\) - (a) For \(p=6 \mathrm{kPa}\), determine the quality of the steam exiting the second stage of the turbine and the thermal efficiency. (b) Plot the quantities of part (a) versus \(p\) ranging from \(4 \mathrm{kPa}\) to \(70 \mathrm{kPa}\).

Short Answer

Expert verified
Calculate enthalpies and entropies using steam tables for different stages. Use isentropic efficiency to find work done and thermal efficiencies. Plot the values for different condenser pressures from 4 kPa to 70 kPa.

Step by step solution

01

- Understand the Problem Statement and Gather Data

Steam is superheated in a supercritical reheat cycle with specified pressures and temperatures for different stages. Given data include pressures and temperatures for different stages, and isentropic efficiencies for the turbine and pump. The steam quality and thermal efficiency calculation need to be repeated for varying condenser pressures (4 kPa to 70 kPa).
02

- Analyze the First Stage of the Turbine

The steam enters the first-stage turbine at 28 MPa and 520 °C. Using steam tables, find the specific enthalpy and entropy of the inlet conditions. The outlet conditions are at 6 MPa and can be found using isentropic efficiency formula and entropy values.
03

- Reheat Process at Constant Pressure

After the first-stage turbine, the steam is reheated to 500 °C at a constant pressure of 6 MPa. Use steam tables to find the specific enthalpy after reheating.
04

- Second Stage of the Turbine

The steam re-enters the turbine after reheating at 6 MPa, 500 °C and expands to the condenser pressure (p = 6 kPa initially). Again, use steam tables and consider isentropic efficiency to find the entropy and quality of the steam exiting the second-stage turbine.
05

- Calculate Efficiency of the Turbine Stages

Combine the enthalpy changes from both stages, taking into account the isentropic efficiency, to find the work done by the turbines. Calculate the heat added during the reheating process and combine it with the work done by the pump to find thermal efficiency.
06

- Vary Condenser Pressure

Repeat the calculations from Steps 2 to 5 for condenser pressures ranging from 4 kPa to 70 kPa. Use tables or suitable software to find enthalpies and entropies for different pressures.
07

- Plot Results

Plot the quality of steam exiting the second stage and thermal efficiency as a function of the condenser pressure from 4 kPa to 70 kPa.

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Key Concepts

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

Isentropic Efficiency
In thermodynamics, isentropic efficiency is a measure of the real-world performance of a device compared to its ideal performance. It's defined as the ratio of the actual work output of the device to the work output if the process were isentropic (i.e., no entropy change).

For turbines, the isentropic efficiency is given by:

\[ \eta_\text{isentropic} = \frac{h_1 - h_2}{h_1 - h_{2s}} \]

Where:
  • \( h_1 \) = specific enthalpy at the inlet
  • \( h_2 \) = specific enthalpy at the actual outlet
  • \( h_{2s} \) = specific enthalpy assuming an isentropic process

In our exercise, the first-stage turbine has an isentropic efficiency of 78%, meaning the actual exit enthalpy would be higher than in an ideal isentropic process due to irreversibilities.
Thermal Efficiency
Thermal efficiency of a power cycle measures how well it converts heat input into work output. It's often the ratio of the net work output of the cycle to the heat input.

For the supercritical reheat cycle in the exercise, the thermal efficiency \( \eta_\text{thermal} \) is calculated using:

\[ \eta_\text{thermal} = \frac{W_{\text{net}}}{Q_{\text{in}}} \]

Where:
  • \( W_{\text{net}} \) = net work output (sum of turbine work minus pump work)
  • \( Q_{\text{in}} \) = total heat added during the cycle

To compute \( W_{\text{net}} \), you'll sum the work done by turbines in both stages and subtract the work required by the pump. Using the enthalpy values from steam tables, the efficiencies of the processes are adjusted accordingly.
Steam Tables
Steam tables are essential tools in thermodynamics, especially when dealing with phase changes and energy calculations in steam cycles. They provide data about thermodynamic properties of water and steam, including:

  • Specific enthalpy \( h \)
  • Specific entropy \( s \)
  • Temperature
  • Pressure
  • Specific volume \( v \)

In the supercritical reheat cycle exercise, steam tables help determine the specific enthalpy and entropy values at given states (pressures and temperatures) throughout the cycle. These properties allow you to calculate work done, heat added, and phase changes, which are crucial for determining efficiency and performance.
Enthalpy
Enthalpy \( h \) is a thermodynamic quantity equivalent to the total heat content of a system. It's given by:

\[ h = u + pv \]

Where:
  • \( u \) = internal energy
  • \( p \) = pressure
  • \( v \) = specific volume

Enthalpy changes play a crucial role in the supercritical reheat cycle, as they allow you to calculate the energy added and work done at different stages. For instance, the enthalpy changes between the inlet and outlet of the turbines and boiler determine the various work and heat quantities.
Entropy
Entropy \( s \) is a measure of disorder or randomness, often associated with the amount of energy unavailable for doing work. It's a critical property in determining the reversibility of thermodynamic processes.

In the supercritical reheat cycle, the isentropic efficiency calculations involve entropy to track the ideal versus real processes. Using steam tables, you find entropy at different states to evaluate the isentropic efficiency:

For the first-stage turbine, the outlet entropy (assuming isentropic process) helps determine the actual enthalpy and, subsequently, the actual work done. The same applies to the second-stage turbine and the pump in the cycle.

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Most popular questions from this chapter

Superheated steam at \(8 \mathrm{MPa}\) and \(480^{\circ} \mathrm{C}\) leaves the steam generator of a vapor power plant. Heat transfer and frictional effects in the line connecting the steam generator and the turbine reduce the pressure and temperature at the turbine inlet to \(7.6 \mathrm{MPa}\) and \(440^{\circ} \mathrm{C}\), respectively. The pressure at the exit of the turbine is \(10 \mathrm{kPa}\), and the turbine operates adiabatically. Liquid leaves the condenser at \(8 \mathrm{kPa}, 36^{\circ} \mathrm{C}\). The pressure is increased to \(8.6\) MPa across the pump. The turbine and pump isentropic efficiencies are \(88 \%\). The mass flow rate of steam is \(79.53 \mathrm{~kg} / \mathrm{s}\). Determine (a) the net power output, in \(\mathrm{kW}\). (b) the thermal efficiency. (c) the rate of heat transfer from the line connecting the steam generator and the turbine, in \(\mathrm{kW}\). (d) the mass flow rate of condenser cooling water, in \(\mathrm{kg} / \mathrm{s}\), if the cooling water enters at \(15^{\circ} \mathrm{C}\) and exits at \(35^{\circ} \mathrm{C}\) with negligible pressure change.

Steam enters the turbine of a vapor power plant at 600 lbfin., \(1000^{\circ} \mathrm{F}\) and exits as a two-phase liquid-vapor mixture at temperature \(T\). Condensate exits the condenser at a temperature \(5^{\circ} \mathrm{F}\) lower than \(T\) and is pumped to \(600 \mathrm{lb} / \mathrm{in}^{2} .\) The turbine and pump isentropic efficiencies are 90 and \(80 \%\), respectively. The net power developed is \(1 \mathrm{MW}\). (a) For \(T=80^{\circ} \mathrm{F}\), determine the steam quality at the turbine exit, the steam mass flow rate, in Ib/h, and the thermal cfficiency. (b) Plot the quantities of part (a) versus \(T\) ranging from \(80 \square\) to \(105^{\circ} \mathrm{F}\).

Water is the working fluid in an ideal regenerative Rankine cycle with one closed feedwater heater. Superheated vapor enters the turbine at \(10 \mathrm{MPa}, 480^{\circ} \mathrm{C}\), and the condenser pressure is \(6 \mathrm{kPa}\). Steam expands through the first-stage turbine where some is extracted and diverted to a closed feedwater heater at \(0.7 \mathrm{MPa}\). Condensate drains from the feedwater heater as saturated liquid at \(0.7 \mathrm{MPa}\) and is trapped into the condenser. The feedwater leaves the heater at \(10 \mathrm{MPa}\) and a temperature equal to the saturation temperature at \(0.7 \mathrm{MPa}\). Determine for the cycle (a) the heat transfer to the working fluid passing through the steam generator, in kJ per kg of steam entering the firststage turbine. (b) the thermal efficiency. (c) the heat transfer from the working fluid passing through the condenser to the cooling water, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of steam entering the first-stage turbine.

Water is the working fluid in a regenerative Rankine cycle with one closed feedwater heater. Steam enters the turbine at \(1400 \mathrm{lb} /\) in. \({ }^{2}\) and \(1000^{\circ} \mathrm{F}\) and expands to \(120 \mathrm{lbt} / \mathrm{in}^{2}\), where some of the steam is extracted and diverted to the closed feedwater heater. The remaining steam expands through the second-stage turbine to the condenser pressure of \(2 \mathrm{lbf}\) in. \({ }^{2}\) Each turbine stage and the pump have isentropic efficiencies of \(85 \%\). Flow through the condenser, closed feedwater heater, and steam generator is at constant pressure. Condensate exiting the feedwater heater as saturated liquid at \(120 \mathrm{lbf} / \mathrm{in}^{2}\) undergoes a throttling process as it passes through a trap into the condenser. The feedwater leaves the heater at \(1400 \mathrm{lbf} / \mathrm{in}^{2}\) and a temperature equal to the saturation temperature at \(120 \mathrm{lbf} / \mathrm{in}^{2}\). The net power output of the cycle is \(1 \times 10^{9} \mathrm{Btu} / \mathrm{h}\). Determine for the cycle (a) the mass flow rate of steam entering the first stage of the turbine, in \(\mathrm{lb} / \mathrm{h}\). (b) the rate of heat transfer, in Btu/h, to the working fluid passing through the steam generator. (c) the thermal efficiency.

A binary vapor cycle consists of two Rankine cycles with steam and ammonia as the working fluids. In the steam cycle, superheated vapor enters the turbine at \(900 \mathrm{lbf} / \mathrm{in}^{2}, 1100^{\circ} \mathrm{F}\), and saturated liquid exits the condenser at \(140^{\circ} \mathrm{F}\). The heat rejected from the steam cycle is provided to the ammonia cycle, producing saturated vapor at \(120^{\circ} \mathrm{F}\), which enters the ammonia turbine. Saturated liquid leaves the ammonia condenser at \(75^{\circ} \mathrm{F}\). Each turbine has an isentropic efficiency of \(90 \%\) and the pumps operate isentropically. The net power output of the binary cycle is \(7 \times 10^{7} \mathrm{Btu} / \mathrm{h}\). (a) Determine the quality at the exit of each turbine, the mass flow rate of each working fluid, in \(\mathrm{lb} / \mathrm{h}\), and the overall thermal efficiency of the binary cycle. (b) Compare the binary cycle performance to that of a single Rankine cycle using water as the working fluid and condensing at \(75^{\circ} \mathrm{F}\). The turbine inlet state, isentropic turbine efficiency, and net power output all remain the same.

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