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Consider a regenerative vapor power cycle with two feedwater heaters, a closed one and an open one. Steam enters the first turbine stage at \(8 \mathrm{MPa}, 480^{\circ} \mathrm{C}\), and expands to \(2 \mathrm{MPa}\). Some steam is extracted at \(2 \mathrm{MPa}\) and fed to the closed feedwater heater. The remainder expands through the second-stage turbine to \(0.3 \mathrm{MPa}\), where an additional amount is extracted and fed into the open feedwater heater, which operates at \(0.3 \mathrm{MPa}\). The steam expanding through the third-stage turbine exits at the condenser pressure of \(8 \mathrm{kPa}\). Feedwater leaves the closed heater at \(205^{\circ} \mathrm{C}, 8 \mathrm{MPa}\), and condensate exiting as saturated liquid at \(2 \mathrm{MPa}\) is trapped into the open heater. Saturated liquid at \(0.3 \mathrm{MPa}\) leaves the open feedwater heater. The net power output of the cycle is \(100 \mathrm{MW}\). If the turbine stages and pumps are isentropic, determine (a) the thermal efficiency. (b) the mass flow rate of steam entering the first turbine, in \(\mathrm{kg} / \mathrm{h}\).

Short Answer

Expert verified
Thermal efficiency calculated from work and heat transfers. Mass flow rate from net power divided by steam work.

Step by step solution

01

Analyzing the Turbine Expansion Stages

First stage: Steam enters at 8 MPa, 480°C and expands to 2 MPa. Extract steam at 2 MPa for closed feedwater heater. Second stage: Remaining steam expands from 2 MPa to 0.3 MPa, where further steam is extracted for open feedwater heater. Third stage: Steam finally expands to condenser pressure of 8 kPa.
02

Determining State Properties at Key Points

Use steam tables or Mollier diagram to determine the properties (enthalpy, entropy) at different states (1 to 10) based on given pressures and temperatures. Specifically, for points 1 (8 MPa, 480°C), 2 (2 MPa), 3 (0.3 MPa), 4 (8 kPa).
03

Calculation of Work and Heat Transfer

Calculate work done by each turbine stage using enthalpy changes (1 to 2, 2 to 3, 3 to 4). Calculate work done by pumps using enthalpy changes for feedwater heaters.
04

Efficiency Calculation

Calculate the total heat added to the system. The thermal efficiency is given by the net work output divided by the heat added.
05

Determining Mass Flow Rate

Using the given net power output (100 MW) and calculated turbine work per kg of steam, determine the mass flow rate by dividing the net power output by the specific work done by the steam (consider all turbine stages).

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Key Concepts

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

Thermal Efficiency
Thermal efficiency is a key measure of performance in a regenerative vapor power cycle. It's defined as the ratio of net work output to the total heat input. In simpler terms, it tells you how much of the heat energy added to the system is converted to useful work.
In this cycle, the process involves stages where steam enters the turbine, expands, and gets reheated. The efficiency in each stage contributes to the overall efficiency. Here’s a quick formula to help:
\[ \text{Thermal Efficiency} (\text{η}) = \frac{W_{net}}{Q_{in}} \times 100 \text{(%)}, \ \text{where,} \ W_{net} = \text{Net work done by the cycle} \ Q_{in} = \text{Total heat added to the system} \]\ In regenerative cycles, using feedwater heaters improves the thermal efficiency by preheating the feedwater before it returns to the boiler. This means less fuel is used to heat the water, improving overall efficiency.
Feedwater Heater
Feedwater heaters are devices used to preheat the water entering the boiler using steam extracted from intermediate stages of a turbine. They come in two types: closed feedwater heaters and open feedwater heaters.
  • Closed Feedwater Heater: This heater allows steam to transfer its heat to the feedwater without mixing with it.

  • Open Feedwater Heater: In this heater, extracted steam mixes directly with the feedwater.
Benefit of using feedwater heaters is that they increase the cycle's thermal efficiency. Preheating the feedwater requires less fuel to heat the water to steam, which means the boiler works less hard.
In the given problem, steam at 2 MPa is extracted and fed into a closed feedwater heater. Another portion is extracted at 0.3 MPa and fed into an open feedwater heater. The final heating occurs before the water reaches the boiler.
Turbine Expansion
Turbine expansion in a regenerative vapor power cycle occurs in multiple stages. Each stage involves steam expanding through the turbine and performing work.
  • First Stage: Steam expands from 8 MPa, 480°C to 2 MPa, with some of the steam extracted for the closed feedwater heater.

  • Second Stage: The remaining steam further expands from 2 MPa to 0.3 MPa. Additional steam is extracted for the open feedwater heater.

  • Third Stage: The remaining steam finally expands to 8 kPa, exiting the turbine at condenser pressure.
At each stage, the extracted steam helps preheat the feedwater, contributing to greater overall efficiency. The energy conversion during these expansions is quantified using enthalpy changes, found in steam tables or Mollier diagrams, and is crucial for calculating overall work done.

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Most popular questions from this chapter

A power plant operates on a regenerative vapor power cycle with one closed feedwater heater. Steam enters the first turbine stage at 120 bar, \(520^{\circ} \mathrm{C}\) and expands to 10 bar, where some of the steam is extracted and diverted to a closed feedwater heater. Condensate exiting the feedwater heater as saturated liquid at 10 bar passes through a trap into the condenser. The feedwater exits the heater at 120 bar with a temperature of \(170^{\circ} \mathrm{C}\). The condenser pressure is \(0.06\) bar. For isentropic processes in each turbine stage and the pump, determine for the cycle (a) the thermal efficiency and (b) the mass flow rate into the first-stage turbine, in \(\mathrm{kg} / \mathrm{h}\), if the net power developed is \(320 \mathrm{MW}\).

Superheated steam at \(18 \mathrm{MPa}, 560^{\circ} \mathrm{C}\), enters the turbine of a vapor power plant. The pressure at the exit of the turbine is \(0.06\) bar, and liquid leaves the condenser at \(0.045\) bar, \(26^{\circ} \mathrm{C}\). The pressure is increased to \(18.2 \mathrm{MPa}\) across the pump. The turbine and pump have isentropic efficiencies of 82 and \(77 \%\), respectively. For the cycle, determine (a) the net work per unit mass of steam flow, in \(\mathrm{kJ} / \mathrm{kg}\). (b) the heat transfer to steam passing through the boiler, in kJ per \(\mathrm{kg}\) of steam flowing. (c) the thermal efficiency. (d) the heat transfer to cooling water passing through the condenser, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of steam condensed.

Vast quantities of water circulate through the condensers of large power plants, exiting at temperatures 10 to \(15^{\circ} \mathrm{C}\) above the ambient temperature. What possible uses could be made of the condenser cooling water? Does this warm water represent a significant resource? What environmental concerns are associated with cooling water? Discuss.

Refrigerant \(134 \mathrm{a}\) is the working fluid in a solar power plant operating on a Rankine cycle. Saturated vapor at \(60^{\circ} \mathrm{C}\) enters the turbine, and the condenser operates at a pressure of 6 bar. The rate of energy input to the collectors from solar radiation is \(0.4 \mathrm{~kW}\) per \(\mathrm{m}^{2}\) of collector surface area. Determine the \(\mathrm{min}\) imum possible solar collector surface area, in \(\mathrm{m}^{2}\), per \(\mathrm{kW}\) of power developed by the plant.

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 \(8.6 \mathrm{MPa}\) 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.

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