/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 39 In an air-standard Brayton cycle... [FREE SOLUTION] | 91Ó°ÊÓ

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In an air-standard Brayton cycle, air from the atmosphere at 1 bar, \(300 \mathrm{~K}\) is compressed to 6 bar, and the maximum cycle temperature is limited to \(1050 \mathrm{~K}\). The mass flow rate of air is \(4 \mathrm{~kg} / \mathrm{s}\). The turbine and the compressor have isentropic efficiencies of \(85 \%\) and \(88 \%\), respectively, take specific heat for air \(\left(c_{p}\right)\) to be \(1.005 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\) and \(k=1.4\). Determine (a) thermal efficiency of the cycle. (b) back work ratio. (c) nower outnut in \(\mathrm{kW}\)

Short Answer

Expert verified
Thermal efficiency: 30.03 %, Back work ratio: 0.58, Net power output: 638.06 kW

Step by step solution

01

- Identify Given Values

Use the given values: - Atmospheric pressure, P1 = 1 bar - Atmospheric temperature, T1 = 300 K - Compressor discharge pressure, P2 = 6 bar - Maximum temperature, T3 = 1050 K - Mass flow rate, m = 4 kg/s - Isentropic efficiency of compressor, η_c = 0.88 - Isentropic efficiency of turbine, η_t = 0.85 - Specific heat, c_p = 1.005 kJ/kg·K - Ratio of specific heats, k = 1.4
02

- Calculate Temperature After Compressor (Isentropic Process)

Using the isentropic relation: T2s / T1 = (P2 / P1)^((k-1)/k) T2s = T1 * (P2 / P1)^((k-1)/k) T2s = 300 K * (6/1)^((1.4-1)/1.4) T2s ≈ 494.14 K
03

- Calculate Actual Temperature After Compressor

Using the isentropic efficiency relation of compressor: η_c = (T2s - T1) / (T2 - T1) T2 = T1 + (T2s - T1) / η_c T2 = 300 K + (494.14 K - 300 K) / 0.88 T2 ≈ 523.11 K
04

- Determine Temperature Before Turbine (Ideal)

Since T3 is given: T3 = 1050 K
05

- Calculate Temperature After Turbine (Isentropic Process)

Using the isentropic relation: T4s / T3 = (P4 / P3)^((k-1)/k) Since P4 = P1, P3 = P2: T4s / 1050 K = (1 / 6)^((1.4-1)/1.4) T4s ≈ 602.43 K
06

- Calculate Actual Temperature After Turbine

Using the isentropic efficiency relation of turbine: η_t = (T3 - T4) / (T3 - T4s) T4 = T3 - η_t * (T3 - T4s) T4 = 1050 K - 0.85 * (1050 K - 602.43 K) T4 ≈ 668.93 K
07

- Calculate Compressor Work

W_c = m * c_p * (T2 - T1) W_c = 4 kg/s * 1.005 kJ/kg·K * (523.11 K - 300 K) W_c ≈ 895.44 kW
08

- Calculate Turbine Work

W_t = m * c_p * (T3 - T4) W_t = 4 kg/s * 1.005 kJ/kg·K * (1050 K - 668.93 K) W_t ≈ 1533.50 kW
09

- Calculate Net Work Output

W_net = W_t - W_c W_net = 1533.50 kW - 895.44 kW W_net ≈ 638.06 kW
10

- Calculate Heat Added

Q_in = m * c_p * (T3 - T2) Q_in = 4 kg/s * 1.005 kJ/kg·K * (1050 K - 523.11 K) Q_in ≈ 2125.62 kW
11

- Calculate Thermal Efficiency

η_thermal = W_net / Q_in * 100 η_thermal = 638.06 kW / 2125.62 kW * 100 η_thermal ≈ 30.03 %
12

- Calculate Back Work Ratio

BWR = W_c / W_t BWR = 895.44 kW / 1533.50 kW BWR ≈ 0.58

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Key Concepts

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

thermal efficiency
Thermal efficiency in a Brayton cycle measures how effectively the cycle converts heat into work. It's a ratio of the net work output and the heat added to the cycle. To find the thermal efficiency (\u03b7_{thermal}), you use the formula: \[ \u03b7_{thermal} = \frac{W_{net}}{Q_{in}} \times 100 \] where \( W_{net} \) is the net work output, and \( Q_{in} \) is the heat added. A higher thermal efficiency means a more efficient engine. In our exercise, it comes out to be approximately 30.03%. This value signifies that only 30.03% of the input energy is converted into useful work, while the rest is wasted.
isentropic process
An isentropic process is one that is both adiabatic (no heat transfer) and reversible. In thermodynamics, it's a key idealization used to analyze cycles. During an isentropic process in the Brayton cycle, entropy remains constant, which aids in calculating temperatures and pressures at various points.
To calculate the temperature after adiabatic compression (T2s) or expansion (T4s), you can use the isentropic relation: \[ \frac{T2s}{T1} = \left( \frac{P2}{P1} \right)^{\frac{k-1}{k}} \] For the turbine, this becomes: \[ \frac{T4s}{T3} = \left( \frac{P4}{P3} \right)^{\frac{k-1}{k}} \] where \( T \) is temperature, \( P \) is pressure, and \( k \) is the specific heat ratio (1.4 for air in this case).
compressor work
Compressor work is the energy required to compress the air from a lower pressure to a higher pressure in the Brayton cycle. It can be calculated using the mass flow rate, specific heat at constant pressure \( c_p \), and the temperature difference.
Using the relation: \[ W_{c} = m \times c_p \times (T2 - T1) \] where \( W_{c} \) is the compressor work in kW, \( m \) is the mass flow rate in kg/s, \( c_p \) is the specific heat capacity at constant pressure, and \( \Delta T \) (\text{T2 - T1}) is the temperature rise through the compressor. Given our values: \[ W_{c} \approx 895.44 \text{ kW} \]
turbine work
Turbine work is the energy produced when high-temperature, high-pressure air expands through the turbine. This expansion drives the turbine blades, producing work. Similar to compressor work, it can be calculated with mass flow rate, specific heat capacity, and temperature drop.
Using: \[ W_{t} = m \times c_p \times (T3 - T4) \] where \( W_{t} \) is the turbine work output in kW, \( T3 \) is the temperature before expansion, and \( T4 \) is the temperature after expansion. With the given values, it results in about 1533.50 kW of turbine work.
back work ratio
The back work ratio (BWR) is an indicator of how much work generated by the turbine is used to drive the compressor. It is the ratio of the compressor work \( W_{c} \) to the turbine work \( W_{t} \).
Mathematically, it is expressed as: \[ BWR = \frac{W_{c}}{W_{t}} \] For the Brayton cycle in our problem, it is approximately 0.58. This implies that 58% of the work produced by the turbine goes back into driving the compressor. A lower BWR is generally desired as it means more net work is available for useful purposes.
specific heat capacity
Specific heat capacity (\( c_p \)) is a measure of the heat energy required to raise the temperature of a unit mass of a substance by one degree Celsius. In the Brayton cycle, the specific heat at constant pressure for air is used to calculate the heat added and removed.
It's vital in formulas like: \[ Q = m \times c_p \times \text{ \Delta T} \] for calculating the heat transfer in and out of the working fluid. For air, \( c_p \) is given as 1.005 kJ/kg·K. This value helps in determining how much energy is needed to heat or cool the air in different parts of the cycle.

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Most popular questions from this chapter

The compression ratio of an air-standard Diesel cycle is 17 and the conditions at the beginning of compression are \(p_{1}=100 \mathrm{kPa}, V_{1}=0.06 \mathrm{~m}^{3}\), and \(T_{1}=300 \mathrm{~K}\). The maximum temperature in the cycle is \(2220 \mathrm{~K}\). Calculate (a) the net work for the cycle, in \(\mathrm{kJ}\). (b) the thermal efficiency. (c) the mean effective pressure, in \(\mathrm{kPa}\) (d) the cutoff ratio.

Air enters the compressor of a gas turbine at \(100 \mathrm{kPa}\), \(300 \mathrm{~K}\). The air is compressed in two stages to \(900 \mathrm{kPa}\), with intercooling to \(300 \mathrm{~K}\) between the stages at a pressure of \(300 \mathrm{kPa}\). The turbine inlet temperature is \(1480 \mathrm{~K}\) and the expansion occurs in two stages, with reheat to \(1420 \mathrm{~K}\) between the stages at a pressure of \(300 \mathrm{kPa}\). The compressor and turbine stage efficiencies are 84 and \(82 \%\), respectively. The net power developed is \(1.8 \mathrm{MW}\). Determine (a) the volumetric flow rate, in \(\mathrm{m}^{3} / \mathrm{s}\), at the inlet of each compressor stage. (b) the thermal efficiency of the cycle. (c) the back work ratio.

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A manufacturing company currently purchases \(2.4 \times\) \(10^{5} \mathrm{MW} \cdot \mathrm{h}\) of electricity annually from the local utility company. An aging boiler on the premises annually provides \(4 \times 10^{8} \mathrm{~kg}\) of process steam at 20 bar. Consider the feasibility of acquiring a cogeneration system to meet these needs. The system would employ a natural gas-fueled gas turbine to produce the electricity and a heat-recovery steam generator to produce the steam. Using thermoeconomic principles, investigate the economic issues that should be considered in making a recommendation about the proposed cogeneration system. Write a report of your findings.

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