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Air enters the compressor of a cold air-standard Brayton cycle with regeneration at \(100 \mathrm{kPa}, 300 \mathrm{~K}\), with a mass flow rate of \(5 \mathrm{~kg} / \mathrm{s}\). The compressor pressure ratio is 9 , and the turbine inlet temperature is \(1320 \mathrm{~K}\). The turbine and compressor each have isentropic efficiencies of \(85 \%\) and the regenerator effectiveness is \(85 \%\). For \(k=1.4\), calculate (a) the thermal efficiency of the cycle. (b) the back work ratio. (c) the net power developed, in \(\mathrm{kW}\). (d) the rate of exergy destruction in the regenerator, in \(\mathrm{kW}\), for \(T_{0}=300 \mathrm{~K}\).

Short Answer

Expert verified
a) 61.5%b) 1.442c) -1708.291 kWd) 564.075 kW

Step by step solution

01

Determine Compressor Outlet Temperature

First, use the isentropic relation to find the outlet temperature of the compressor: \[ T_{2s} = T_1 \left( \frac{P_2}{P_1} \right)^{\frac{k-1}{k}} \rightarrow T_{2s} = 300 \left( \frac{900}{100} \right)^{\frac{0.4}{1.4}} = 300 \times 3.737 = 1121.1 \space K \] Since the compressor is not isentropic, use the isentropic efficiency to find the actual outlet temperature: \[ \eta_c = \frac{T_{2s} - T_1}{T_2 - T_1} \rightarrow 0.85 = \frac{1121.1 - 300}{T_2 - 300} \rightarrow T_2 = \frac{1121.1 - 300}{0.85} + 300 = 1412.94 \space K \]
02

Determine Turbine Outlet Temperature

Use the isentropic relation to find the outlet temperature of the turbine if it were isentropic:\[ T_{4s} = T_3 \left( \frac{P_4}{P_3} \right)^{\frac{k-1}{k}} \rightarrow T_{4s} = 1320 \left( \frac{100}{900} \right)^{\frac{0.4}{1.4}} = 1320 \times 0.267 = 352.44 \space K \] Applying the isentropic efficiency to find the actual outlet temperature: \[ \eta_t = \frac{T_3 - T_{4s}}{T_3 - T_4} \rightarrow 0.85 = \frac{1320 - 352.44}{1320 - T_4} \rightarrow T_4 = 1320 - \frac{1320 - 352.44}{0.85} = 548.28 \space K \]
03

Determine Max Temperature for Regenerator

The maximum possible temperature leaving the regenerator is the outlet temperature from the turbine: \[ T_{5} = T_4 = 548.28 \space K \]
04

Determine Temperature Before Combustion

The temperature before the combustion chamber after the regenerator is: \[ T_{5} = T_2 + \varepsilon (T_4 - T_2) \rightarrow T_{5} = 1412.94 + 0.85 (548.28 - 1412.94) = 675.78 \space K \]
05

Calculate the Thermal Efficiency

The thermal efficiency of the cycle can be calculated by: \[ \eta_{th} = 1 - \frac{\dot{Q}_{out}}{\dot{Q}_{in}} \rightarrow \eta_{th} = 1 - \frac{c_p (T_4 - T_1)}{c_p (T_3 - T_2)} \] Assuming specific heat capacity at constant pressure, c_p, is constant, it cancels out. So the efficiency is: \[ \eta_{th} = 1 - \frac{548.28 - 300}{1320 - 675.78} = 1 - \frac{248.28}{644.22} = 1 - 0.385 = 0.615 \text{ or } 61.5\% \]
06

Calculate the Back Work Ratio

The back work ratio is the ratio of the work done by the compressor to the work generated by the turbine: \[ BWR = \frac{W_c}{W_t} = \frac{c_p (T_2 - T_1)}{c_p (T_3 - T_4)} = \frac{1412.94 - 300}{1320 - 548.28} = \frac{1112.94}{771.72} = 1.442 \]
07

Calculate the Net Power Developed

The net power developed can be found by subtracting the compressor work from the turbine work: \[ \dot{W}_{net} = \dot{W}_t - \dot{W}_c = \dot{m} \cdot c_p \cdot ((T_3 - T_4) - (T_2 - T_1)) \] Using an average specific heat at constant pressure, c_p, of 1005 J/(kg·K), and mass flow rate \( \dot{m} = 5 \) kg/s: \[ \dot{W}_{net} = 5 \times 1005 ( (1320 - 548.28) - (1412.94 - 300) ) = 5 \times 1005 ( 771.72 - 1112.94) = 5 \times 1005 \times (-341.22) = -1708291.5 \text{ W or -1708.291 kW} \]
08

Calculate Rate of Exergy Destruction

The rate of exergy destruction in the regenerator is given by: \[ \dot{E}_{D_{regen}} = \dot{m} c_p (T_4 - T_5) \left( 1 - \frac{T_0}{T_4} \right) \rightarrow \dot{E}_{D_{regen}} = 5 \cdot 1005 \cdot (548.28 - 300) \left( 1 - \frac{300}{548.28} \right) \rightarrow \dot{E}_{D_{regen}} = 5 \cdot 1005 \cdot 248.28 \cdot \left( 1 - 0.547 \right) \rightarrow \dot{E}_{D_{regen}} = 5 \cdot 1005 \cdot 248.28 \cdot 0.453 = 564075.027 \text{ W or 564.075 kW} \]

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Key Concepts

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

Isentropic Efficiency
Isentropic efficiency is a measure of how close a real process comes to the ideal, isentropic process. The isentropic efficiency of a device, like a compressor or turbine, can be defined as the ratio of the actual work output or input to the work output or input of an ideal, isentropic process.

For compressors: \ \ \ \[ \ \eta_c = \frac{T_{2s} - T_1}{T_2 - T_1} \ \]
For turbines: \ \ \ \[ \ \eta_t = \frac{T_3 - T_{4s}}{T_3 - T_4} \ \]
Where \(T_{2s}\) and \(T_{4s}\) are the temperatures at the compressor and turbine outlets, respectively, for an isentropic process. The actual outlet temperatures \(T_2\) and \(T_4\) are higher and lower, respectively, because real processes are not perfectly efficient. By improving these efficiencies, we reduce energy losses, making the Brayton cycle more effective.
Thermal Efficiency
Thermal efficiency is a dimensionless measure of how well a heat engine converts heat from the combustion of fuel into work. For the Brayton cycle, it is essential to understand both the heat added (\(\dot{Q}_{in}\)) and the heat rejected (\(\dot{Q}_{out}\)).

The thermal efficiency \ \(\eta_{th}\) is then given by: \ \ \ \[ \ \eta_{th} = 1 - \frac{\dot{Q}_{out}}{\dot{Q}_{in}}\ \]
Here we find the amount of heat rejected and compare it to the heat added, resulting in a measure of efficiency. For the Brayton cycle, the specific formula applicable can be simplified to focus on temperature differences: \ \ \ \ \[\ \eta_{th} = 1 - \frac{T_4 - T_1}{T_3 - T_2} = 1 - \frac{248.28}{644.22} = 61.5\%\ \]
This result highlights how efficient the cycle is at converting fuel energy into useful work.
Back Work Ratio
The back work ratio is crucial in the Brayton cycle because it measures the fraction of the turbine's work output used to drive the compressor. Unlike some cycles where minimal work is required for compression, the Brayton cycle often has a significant back work ratio.

The back work ratio (\(BWR\)) is given by: \ \ \[ \ \frac{W_c}{W_t} = \frac{c_p (T_2 - T_1)}{c_p (T_3 - T_4)} \]
In our problem: \ \ \[ \BWR = \frac{1412.94 - 300}{1320 - 548.28} = 1.442 \ \]
This ratio tells us that a substantial portion (44.2%) of the turbine's work is needed to drive the compressor, impacting the net power output of the cycle.
Exergy Destruction
Exergy destruction measures the irreversibility within a system. In the regenerator of a Brayton cycle, this translates to the inherent losses due to inefficiencies. This is vital for improving system efficiency, as it pinpoints where improvements can be made to reduce waste.

The rate of exergy destruction in the regenerator is given by: \ \ \[\ \dot{E}_{D_{regen}} = \dot{m} \cdot c_p \cdot (T_4 - T_5) \left( 1 - \frac{T_0}{T_4} \right) \]
Substituting the values: \ \ \[\ \dot{E}_{D_{regen}} = 5 \cdot 1005 \cdot (548.28 - 300) \left( 1 - \frac{300}{548.28} \right) = 564.075 \,\text{kW} \]
This considerable destruction value highlights the inefficiency in the regenerator. Understanding and reducing exergy destruction is essential for enhancing the overall cycle efficiency.

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Most popular questions from this chapter

How do internal and external combustion engines differ?

Carbon dioxide is contained in a large tank, initially at \(700 \mathrm{kPa}, 450 \mathrm{~K}\). The gas discharges through a converging nozzle to the surroundings, which are at \(101.3 \mathrm{kPa}\) and the pressure in the tank drops. Estimate the pressure in the tank, in \(\mathrm{kPa}\), when the flow first ceases to be choked.

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Air enters the compressor of a simple gas turbine at \(100 \mathrm{kPa}, 298 \mathrm{~K}\), and exits at \(700 \mathrm{kPa}, 550 \mathrm{~K}\). The air enters the turbine at \(700 \mathrm{kPa}, 1120 \mathrm{~K}\) and expands to \(100 \mathrm{kPa}, 770 \mathrm{~K}\). The compressor and turbine operate adiabatically, and kinetic and potential energy effects are negligible. On the basis of an air-standard analysis, (a) develop a full accounting of the net exergy increase of the air passing through the gas turbine combustor, in \(\mathrm{kJ} / \mathrm{kg}\). (b) devise and evaluate an exergetic efficiency for the gas turbine cycle. Let \(T_{0}=298 \mathrm{~K}, p_{0}=100 \mathrm{kPa}\).

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