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Air enters a turbine operating at steady state at 6 bar and \(1100 \mathrm{~K}\) and expands isentropically to a state where the temperature is \(700 \mathrm{~K}\). Employing the ideal gas model and ignoring kinetic and potential energy changes, determine the pressure at the exit, in bar, and the work, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of air flowing, using (a) data from Table A-22. (b) \(I T\). (c) a constant specific heat ratio from Table A-20 at the mean temperature, \(900 \mathrm{~K}\). (d) a constant specific heat ratio from Table A-20 at \(300 \mathrm{~K}\).

Short Answer

Expert verified
Using Table A-22, determine matching entropy values to find exit pressure. Use enthalpy values to compute work. Repeat with ideal gas tables, mean temperature, and 300 K ratios.

Step by step solution

01

Understand the Problem

Identify given data and what needs to be found. Air enters a turbine at 6 bar and 1100 K and expands isentropically to 700 K. We need to determine the exit pressure and work per kg of air using various approaches.
02

Use Table A-22 for Isentropic Conditions

Use the data from Table A-22 to identify the specific enthalpies and entropies at the given temperatures. The isentropic relation means that entropy at inlet conditions equals entropy at exit conditions.
03

Step 3a: Determine Pressure Using Table A-22

Find entropy values for 1100 K and 700 K from Table A-22. Using isentropic conditions, match entropy values to find the corresponding pressure.
04

Step 3b: Calculate Work Using Table A-22

Using enthalpy values from Table A-22, apply the energy balance equation for adiabatic turbines: \(W = h_{\text{in}} - h_{\text{out}}\)
05

Use Ideal Gas Tables (IT)

Use ideal gas tables to find the specific enthalpies at 1100 K and 700 K. Compute work done with the same energy balance equation as in Step 3b.
06

Use Constant Specific Heat Ratio at Mean Temperature

At mean temperature 900 K, from Table A-20, use the ratio of specific heats ( k = c_p/c_v) to find pressure relation:\(\frac{p_2}{p_1} = \left(\frac{T_2}{T_1}\right)^{\frac{k}{k-1}}\). Then calculate work: \(W = c_p (T_1 - T_2)\)
07

Use Constant Specific Heat Ratio at 300 K

Repeat Step 5 but using the specific heat ratio from Table A-20 at 300 K.
08

Summarize Results

Compare exit pressures and work done per kg air computed using different methods.

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Key Concepts

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

Ideal Gas Model
An important concept in thermodynamics is the ideal gas model. This model simplifies the analysis of gases by assuming they behave ideally. In simple terms, an ideal gas follows the equation of state \(PV = nRT\), where \(P\) is pressure, \(V\) is volume, \(n\) is the number of moles, \(R\) is the universal gas constant, and \(T\) is temperature. This model is highly useful when analyzing turbines, compressors, and other components in thermodynamic cycles. It allows for straightforward calculations of properties like specific enthalpy and specific entropy. In our exercise, we treat air as an ideal gas to determine the pressure and work output of the turbine during isentropic expansion from 1100 K to 700 K.
Specific Enthalpies
Specific enthalpy (\(h\)) is a thermodynamic property that combines internal energy and pressure-volume work. It is defined as \(h = u + Pv\), where \(u\) is the specific internal energy and \(Pv\) represents the flow work. When considering an ideal gas, specific enthalpy is typically a function of temperature. In practical applications, tables like Table A-22 provide specific enthalpies at various temperatures. For instance, in our scenario, we use these tables to find the enthalpy values for air at 1100 K and 700 K. This information is crucial for calculating the work done by the turbine using the relation \(W = h_{\text{in}} - h_{\text{out}}\).
Specific Heat Ratio
The specific heat ratio, also known as the adiabatic index (\(k\)), is the ratio of specific heats at constant pressure (\(c_p\)) to specific heats at constant volume (\(c_v\)). Mathematically, it’s given by \(k = \frac{c_p}{c_v}\). This ratio is key in determining the behavior of gases during adiabatic processes, where no heat is transferred. For an isentropic expansion, like in our turbine exercise, the pressure and temperature relationship can be found using \(\frac{p_2}{p_1} = \left(\frac{T_2}{T_1}\right)^{\frac{k}{k-1}}\). By knowing \(k\), we can derive exit pressure and further use this in calculating work output under different conditions.
Isentropic Relations
Isentropic processes, where entropy remains constant, are key in analyzing adiabatic turbines. For an isentropic process in an ideal gas, the entropy change \(\Delta s = 0\). This means \(s_{\text{in}} = s_{\text{out}}\). Using isentropic relations helps simplify the calculations of state changes. The relation \(\frac{T_2}{T_1} = \left(\frac{p_2}{p_1}\right)^{\frac{k-1}{k}}\) links temperature and pressure during isentropic processes. It should be noted this relationship is derived using the ideal gas model and the adiabatic process assumption. In practical applications, as seen in our exercise, it provides a pathway to calculate the unknown exit pressure after expansion.
Energy Balance Equation
In thermodynamic analysis of turbines, the energy balance equation is a fundamental tool. For an adiabatic turbine, which assumes no heat loss (\(Q = 0\)), the energy balance simplifies to \(W = h_{\text{in}} - h_{\text{out}}\). Here, \(h_{\text{in}}\) and \(h_{\text{out}}\) are the specific enthalpies at the inlet and outlet respectively. This equation reflects the work done per kilogram of air passing through the turbine. This is critical as it directly provides insight into the turbine's performance. For accurate computation, specific enthalpy values are obtained from tables or ideal gas relations. In the exercise given, we use the energy balance equation to calculate work output under various conditions using data from tables and ideal gas properties.

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Most popular questions from this chapter

An inventor claims to have conceived of a second lawchallenging heat engine. (See H. Apsden, "The Electronic Heat Engine," Proceedings 27th International Energy Conversion Engineering Conference, 4.357-4.363, 1992. Also see U.S. Patent No. 5,101,632.) By artfully using mirrors the heat engine would "efficiently convert abundant environmental heat energy at the ambient temperature to electricity." Write a paper explaining the principles of operation of the device. Does this invention actually challenge the second law of thermodynamics? Does it have commercial promise? Discuss,

Steam enters a turbine operating at steady state at a pressure of \(3 \mathrm{MPa}\), a temperature of \(400^{\circ} \mathrm{C}\), and a velocity of \(160 \mathrm{~m} / \mathrm{s}\). Saturated vapor exits at \(100^{\circ} \mathrm{C}\), with a velocity of \(100 \mathrm{~m} / \mathrm{s}\). Heat transfer from the turbine to its surroundings takes place at the rate of \(30 \mathrm{~kJ}\) per kg of steam at a location where the average surface temperature is \(350 \mathrm{~K}\). (a) For a control volume including only the turbine and its contents, determine the work developed, in \(\mathrm{kJ}\), and the rate at which entropy is produced, in \(\mathrm{kJ} / \mathrm{K}\), each per \(\mathrm{kg}\) of steam flowing. (b) The steam turbine of part (a) is located in a factory where the ambient temperature is \(27^{\circ} \mathrm{C}\). Determine the rate of entropy production, in \(\mathrm{kJ} / \mathrm{K}\) per \(\mathrm{kg}\) of steam flowing, for an enlarged control volume that includes the turbine and enough of its immediate surroundings so that heat transfer takes place from the control volume at the ambient temperature. Explain why the entropy production value of part (b) differs from that calculated in part (a).

A patent application describes a device that at steady state receives a heat transfer at the rate \(1 \mathrm{~kW}\) at a temperature of \(167^{\circ} \mathrm{C}\) and generates electricity. There are no other energy transfers. Does the claimed performance violate any principles of thermodynamics? Explain.

A cylindrical rod of length \(L\) insulated on its lateral surface is initially in contact at one end with a wall at temperature \(T_{\mathrm{H}}\) and at the other end with a wall at a lower temperature \(T_{\mathrm{C}}\). The temperature within the rod initially varies linearly with position \(z\) according to $$ T(z)=T_{\mathrm{H}}-\left(\frac{T_{\mathrm{H}}-T_{\mathrm{C}}}{L}\right) z $$ The rod is then insulated on its ends and eventually comes to a final equilibrium state where the temperature is \(T_{\mathrm{f}}\). Evaluate \(T_{\mathrm{f}}\) in terms of \(T_{\mathrm{H}}\) and \(T_{\mathrm{C}}\) and show that the amount of entropy produced is $$ \sigma=m c\left(1+\ln T_{\mathrm{f}}+\frac{T_{\mathrm{C}}}{T_{\mathrm{H}}-T_{\mathrm{C}}} \ln T_{\mathrm{C}}-\frac{T_{\mathrm{H}}}{T_{\mathrm{H}}-T_{\mathrm{C}}} \ln T_{\mathrm{H}}\right) $$ where \(c\) is the specific heat of the rod.

A piston-cylinder assembly initially contains \(0.1 \mathrm{~m}^{3}\) of carbon dioxide gas at \(0.3\) bar and \(400 \mathrm{~K}\). The gas is compressed isentropically to a state where the temperature is \(560 \mathrm{~K}\). Employing the ideal gas model and neglecting kinetic and potential energy effects, determine the final pressure, in bar, and the work in \(\mathrm{kJ}\), using (a) data from Table A-23. (b) \(I T\) (c) a constant specific heat ratio from Table A-20 at the mean temperature, \(480 \mathrm{~K}\). (d) a constant specific heat ratio from Table A-20 at \(300 \mathrm{~K}\).

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