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Water is the working fluid in an ideal Rankine cycle. Saturated vapor enters the turbine at \(16 \mathrm{MPa}\), and the condenser pressure is \(8 \mathrm{kPa}\). The mass flow rate of steam entering the turbine is \(120 \mathrm{~kg} / \mathrm{s}\). Determine (a) the net power developed, in \(k \mathrm{~W}\). (b) the rate of heat transfer to the steam passing through the boiler, in \(\mathrm{kW}\). (c) the thermal efficiency. (d) the mass flow rate of condenser cooling water, in \(\mathrm{kg} / \mathrm{s}\), if the cooling water undergoes a temperature increase of \(18^{\circ} \mathrm{C}\) with negligible pressure change in passing through the condenser.

Short Answer

Expert verified
Net power: Calculate turbine work minus pump work. Heat transfer: Find enthalpy increase in the boiler. Thermal efficiency: ratio of net power to heat added. Cooling water mass flow: Use condenser heat rejected and temperature rise.

Step by step solution

01

- Determine state points using steam tables

Identify the properties of the steam at different state points in the Rankine cycle using steam tables. At the turbine inlet (State 1), steam is at 16 MPa and saturated vapor. At the condenser outlet (State 4), steam is at 8 kPa and saturated liquid. Use relevant steam tables to find enthalpies and entropies at these points.
02

- Calculate turbine work (W_t)

Using State 1 and State 2 (exiting turbine), apply the first law of thermodynamics and assume isentropic expansion: \[ s_1 = s_2 \] Find the enthalpy at State 2 from the steam tables and compute the turbine work: \[ W_t = \frac{(\text{h}_1 - \text{h}_2) \times \text{m}}{1000} \] where h_1 and h_2 are the enthalpies at States 1 and 2 respectively, and m is the mass flow rate.
03

- Calculate pump work (W_p)

For the pump work, use the enthalpy at the condenser outlet (State 4) and the boiler inlet (State 3), assuming isentropic compression: \[ W_p = \frac{(\text{h}_3 - \text{h}_4) \times \text{m}}{1000} \]
04

- Calculate net power developed

The net power developed is the difference between the turbine work and the pump work. \[ W_{net} = W_t - W_p \]
05

- Calculate heat transfer rate to the boiler (Q_in)

Heat transfer rate to the boiler is the enthalpy increase from State 2 to State 1: \[ Q_{in} = \frac{(\text{h}_1 - \text{h}_3) \times \text{m}}{1000} \]
06

- Calculate thermal efficiency

Thermal efficiency is given by the ratio of net power to the heat added: \[ \text{Efficiency} = \frac{W_{net}}{Q_{in}} \]
07

- Calculate mass flow rate of condenser cooling water

Use the heat rejected in the condenser and the temperature rise of the cooling water to find the mass flow rate: \[ Q_{out} = \frac{(\text{h}_2 - \text{h}_3) \times \text{m}}{1000} \] Then, \[ \text{mass flow rate} = \frac{Q_{out}}{ \text{c} \times \text{ΔT}} \] where c is the specific heat capacity of water (4.18 kJ/kg°C) and ΔT is the temperature increase.

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Key Concepts

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

steam tables
Steam tables are an essential tool in thermodynamics, especially for analyzing the Rankine cycle. These tables provide properties of water and steam, such as temperature, pressure, enthalpy, and entropy at various states. They help us identify the properties of steam at different cycle points.
For instance, in the exercise, we use steam tables to find the enthalpies and entropies at the turbine inlet (State 1) and the condenser outlet (State 4). Knowing these values is crucial to calculating work done by the turbine and the heat transfer rates. Steam tables ensure accurate and consistent results, allowing us to solve complex thermodynamic problems efficiently.
isentropic expansion
Isentropic expansion is a theoretical process where entropy remains constant. This concept is especially useful in analyzing turbines in the Rankine cycle.
During isentropic expansion, the steam expands within the turbine without any entropy change, meaning the process is both adiabatic and reversible. This simplifies calculations as we assume \(s_1 = s_2\). Using this assumption, we can find the enthalpy at the exit of the turbine (State 2) using steam tables. This enthalpy is crucial for calculating the turbine work. Isentropic processes highlight ideal conditions, helping us understand real-world deviations and improving turbine designs.
thermal efficiency
Thermal efficiency is a measure of how well a thermodynamic cycle converts heat into work. For the Rankine cycle, we determine it by taking the ratio of the net work output to the heat input:
\[ \text{Efficiency} = \frac{W_{net}}{Q_{in}} \]\br>The thermal efficiency helps us understand the effectiveness of the cycle. A higher efficiency means more useful work is generated from the heat added. In the exercise, after finding the net power developed and the heat transfer rate into the boiler, we use these values to calculate the cycle's thermal efficiency. This efficiency is vital for evaluating the performance of power plants and improving their designs.
enthalpy
Enthalpy is a property that combines internal energy with the product of pressure and volume. It is denoted by \(H\) and plays a crucial role in energy transfer calculations in thermodynamics. Enthalpy changes account for the work done and heat transfer in processes.
For our Rankine cycle, we use enthalpy values at various states to determine the work produced by the turbine and the heat added in the boiler. For example, the turbine work depends on enthalpy difference \(h_1 - h_2\) and the boiler heat addition on \(h_1 - h_3\). Steam tables are handy for finding these enthalpy values for saturated and superheated states. Understanding enthalpy changes is key to solving energy balance problems in cycles.
mass flow rate
Mass flow rate measures how much mass passes through a point in a system per unit time, usually expressed in kg/s. In the exercise, the mass flow rate of steam entering the turbine is 120 kg/s. We use this rate in various calculations including work done and heat transfer.
For instance, the net power developed by the turbine is found using:
\[ W_t = \frac{(\text{h}_1 - \text{h}_2) \times \text{m}}{1000} \]\br>where \(m\) is the mass flow rate. Similarly, when calculating the mass flow rate of condenser cooling water, knowing the heat rejected and the specific heat capacity, we determine the cooling water flow needed to achieve a specific temperature rise. Mass flow rate is a crucial parameter in designing and analyzing thermodynamic systems.

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Most popular questions from this chapter

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.

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.

Water is the working fluid in an ideal regenerative Rankine cycle with one open feedwater heater. Superheated vapor enters the first-stage turbine at \(16 \mathrm{MPa}, 560^{\circ} \mathrm{C}\), and the condenser pressure is \(8 \mathrm{kPa}\). The mass flow rate of steam entering the first-stage turbine is \(120 \mathrm{~kg} / \mathrm{s}\). Steam expands through the first-stage turbine to \(1 \mathrm{MPa}\) where some of the steam is extracted and diverted to an open feedwater heater operating at \(1 \mathrm{MPa}\). The remainder expands through the second-stage turbine to the condenser pressure of \(8 \mathrm{kPa}\). Saturated liquid exits the feedwater heater at \(1 \mathrm{MPa}\). Determine (a) the net power developed, in \(\mathrm{kW}\). (b) the rate of heat transfer to the steam passing through the boiler, in \(\mathrm{kW}\). (c) the thermal efficiency. (d) the mass flow rate of condenser cooling water, in \(\mathrm{kg} / \mathrm{s}\), if the cooling water undergoes a temperature increase of \(18^{\circ} \mathrm{C}\) with negligible pressure change in passing through the condenser.

Water is the working fluid in a Rankine cycle. Superheated vapor enters the turbine at \(8 \mathrm{MPa}, 560^{\circ} \mathrm{C}\) with a mass flow rate of \(7.8 \mathrm{~kg} / \mathrm{s}\) and exits at \(8 \mathrm{kPa}\). Saturated liquid enters the pump at \(8 \mathrm{kPa}\). The isentropic turbine efficiency is \(88 \%\), and the isentropic pump efficiency is \(82 \%\). Cooling water enters the condenser at \(18^{\circ} \mathrm{C}\) and exits at \(36^{\circ} \mathrm{C}\) with no significant change in pressure. Determine (a) the net power developed, in \(\mathrm{kW}\). (b) the thermal efficiency. (c) the mass flow rate of cooling water, in \(\mathrm{kg} / \mathrm{s}\).

In a cogeneration system, a Rankine cycle operates with steam entering the turbine at a rate of \(15 \mathrm{lb} / \mathrm{s}\) at \(1000 \mathrm{lbf}^{2} \mathrm{in}^{2}\), \(800^{\circ} \mathrm{F}\), and a condenser pressure of \(200 \mathrm{lbf} / \mathrm{in}^{2}\). The isentropic turbine efficiency is \(85 \%\) while the pump operates isentropically. Energy rejected by the condensing steam is transferred to a separate process stream of water entering at \(280^{\circ} \mathrm{F}, 150 \mathrm{lbf} / \mathrm{in}^{2}\) and exiting as saturated vapor at \(150 \mathrm{lbt} / \mathrm{in}^{2}\) Determine the mass flow rate, in lb/s, for the process stream. Based on the increase in exergy of the steam passing through the steam generator, devise and evaluate an exergetic efficiency for the overall cogeneration system. Let \(T_{0}=70^{\circ} \mathrm{F}\), \(p_{0}=14.7 \mathrm{lbf} / 1 \mathrm{in}^{2}\)

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