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Methane \(\left(\mathrm{CH}_{4}\right)\) undergoes an isentropic expansion from an initial state where the temperature is \(1000 \mathrm{~K}\) and the pressure is 5 bar to a final state where the temperature is \(T\) and the pressure is \(p\). Using the ideal gas model together with \(\bar{c}_{\mathrm{p}}(T)\) from Table A-21, determine (a) \(p\) when \(T=500 \mathrm{~K}\) (b) \(T\) when \(p=1\) bar. (c) Check the results of parts (a) and (b) using \(I T\).

Short Answer

Expert verified
(a) p = 4.365 bar, (b) T = 45 K

Step by step solution

01

Identify Initial and Final States

The initial state of the methane is given as: \(T_1 = 1000 \mathrm{~K}\) and \(p_1 = 5\) bar. The final state variables are \(T\) and \(p\). Two scenarios are provided: one where \(T_2 = 500 \mathrm{~K}\) and another where \(p_2 = 1\) bar.
02

Understand Isentropic Relation

For an isentropic process of an ideal gas, we can use the relation: \[\left(\frac{T_2}{T_1}\right)^{\frac{\bar{R}}{\bar{c}_p(T)}} = \frac{p_2}{p_1}\] where \(\bar{R}=8.314 \frac{J}{mol \cdot K}\) for methane and \(\bar{c}_p(T)\) is the specific heat capacity at constant pressure, which is a function of temperature.
03

Calculate \(p_2\) for \(T_2 = 500 \mathrm{~K}\)

Using the specific heat capacity from Table A-21, we find \(\bar{c}_p(1000 \mathrm{~K}) = 35.1 \frac{J}{mol \cdot K}\) and \(\bar{c}_p(500 \mathrm{~K}) = 25.1 \frac{J}{mol \cdot K}\). For an approximation, using average \(\bar{c}_p\), we can take \(\bar{c}_p = 30.1 \frac{J}{mol \cdot K}\). Substitute into the isentropic relation: \[ \left( \frac{500}{1000} \right)^{\frac{8.314}{30.1}} = \frac{p_2}{5}\]. Therefore, solving for \(p_2\): \[ p_2 = 5 \times \left( \frac{1}{2} \right)^{\frac{8.314}{30.1}} = 5 \times 0.873 = 4.365 \text{ bar} \]
04

Calculate \(T_2\) for \(p_2 = 1 \text{ bar}\)

Using the same isentropic relation: \[\left( \frac{T_2}{1000} \right)^{\frac{8.314}{30.1}} = \frac{1}{5}\]. Solving for \(T_2\): \[ \left( \frac{T_2}{1000} \right)^{0.276} = 0.2 \]. Thus: \[\frac{T_2}{1000} = 0.2^{3.62}\]. So, \[ T_2 = 1000 \times 0.0448 = 45 \text{ K} \].
05

Validate Results using Information Technology (I T)

Use software or online calculators for thermodynamic properties of methane and the isentropic process to validate intermediate steps. Compare the calculated pressure and temperature with the result from the steps.

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Key Concepts

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

ideal gas model
To understand the isentropic expansion in this exercise, we first need to grasp the *Ideal Gas Model*. This model assumes that gases consist of a vast number of very small particles moving in random directions and that these particles do not interact except for perfectly elastic collisions.
In the context of the Ideal Gas Law, the equation is: \[ PV = nRT \] where
  • \(P\) is the pressure,
  • \(V\) is the volume,
  • \(n\) is the amount of substance,
  • \(R\) is the ideal gas constant,
  • \(T\) is the absolute temperature.
Here, methane can be treated as an ideal gas, making use of this law crucial for solving related problems.
specific heat capacity
*Specific Heat Capacity* is another essential concept for this exercise. It quantifies the amount of heat required to change the temperature of a unit mass of a substance by one degree Celsius. For gases, we often talk about the specific heat capacity at constant pressure, denoted as \( \bar{c}_p(T) \).
For methane, \( \bar{c}_p(T) \) can vary with temperature. For example, in the given solution:
  • \( \bar{c}_p(1000 \text{ K}) = 35.1 \frac{J}{mol \cdot K} \)
  • \( \bar{c}_p(500 \text{ K}) = 25.1 \frac{J}{mol \cdot K} \)
By averaging these values, we use \( \bar{c}_p = 30.1 \frac{J}{mol \cdot K} \). This approximation simplifies calculations for problems involving temperature changes and isentropic relations.
thermodynamic properties
*Thermodynamic Properties* describe the fundamental aspects of substances that dictate the behavior in thermodynamic systems. These include temperature, pressure, volume, internal energy, and entropy.
For this problem, we focus on the properties of methane during the isentropic expansion process. Key properties are:
  • Initial and final temperatures \( T_1 \) and \( T_2 \)
  • Initial and final pressures \( p_1 \) and \( p_2 \)
Thermodynamic relationships help us connect these properties, as seen in the isentropic process equations.
isentropic process
Finally, understanding the *Isentropic Process* is vital. This is a thermodynamic process where entropy remains constant. For an ideal gas undergoing an isentropic process, relations between temperature and pressure are described by the equation: \[ \frac{T_2}{T_1} = \frac{p_2}{p_1}^{\frac{\bar{R}}{\bar{c}_p(T)}} \textrm{with } \bar{R} = 8.314 \frac{J}{mol \bullet K} \] In this exercise involving methane, this equation allowed us to solve for unknown pressures and temperatures in different cases:
  • When \( T_2 = 500 \text{ K} \)
  • When \( p_2 = 1 \text{ bar} \)
Such calculations underline the importance of understanding isentropic processes in thermodynamics.

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Most popular questions from this chapter

Steam enters a horizontal \(15-\mathrm{cm}\)-diameter pipe as a saturated vapor at 5 bar with a velocity of \(10 \mathrm{~m} / \mathrm{s}\) and exits at \(4.5\) bar with a quality of \(95 \%\). Heat transfer from the pipe to the surroundings at \(300 \mathrm{~K}\) takes place at an average outer surface temperature of \(400 \mathrm{~K}\). For operation at steady state, determine (a) the velocity at the exit, in \(\mathrm{m} / \mathrm{s}\). (b) the rate of heat transfer from the pipe, in \(\mathrm{kW}\). (c) the rate of entropy production, in \(\mathrm{kW} / \mathrm{K}\), for a control volume comprising only the pipe and its contents. (d) the rate of entropy production, in \(\mathrm{kW} / \mathrm{K}\), for an enlarged control volume that includes the pipe and enough of its immediate surroundings so that heat transfer from the control volume occurs at \(300 \mathrm{~K}\). Why do the answers of parts (c) and (d) differ?

A quantity of liquid water undergoes a process from \(80^{\circ} \mathrm{C}\), 5 MPa to saturated liquid at \(40^{\circ} \mathrm{C}\). Determine the change in specific entropy, in \(\mathrm{kJ} / \mathrm{kg} \cdot \mathrm{K}\), using (a) Tables A-2 and A-5. (b) saturated liquid data only from Table A-2. (c) the incompressible liquid model with a constant specific heat from Table A-19. (d) \(I T\).

A reversible refrigeration cycle \(\mathrm{R}\) and an irreversible refrigeration cycle I operate between the same two reservoirs and each removes \(Q_{\mathrm{C}}\) from the cold reservoir. The net work input required by \(\mathrm{R}\) is \(W_{\mathrm{R}}\), while the net work input for \(\mathrm{I}\) is \(W_{\mathrm{I}}\). The reversible cycle discharges \(Q_{\mathrm{H}}\) to the hot reservoir, while the irreversible cycle discharges \(Q_{\mathrm{H}}^{\prime}\). Show that \(W_{1}>W_{\mathrm{R}}\) and \(Q_{\mathrm{H}}^{\prime}>Q_{\mathrm{H}}\).

Water is to be pumped from a lake to a reservoir located on a bluff \(290 \mathrm{ft}\) above. According to the specifications, the piping is Schedule 40 steel pipe having a nominal diameter of 1 inch and the volumetric flow rate is \(10 \mathrm{gal} / \mathrm{min}\). The total length of pipe is \(580 \mathrm{ft}\). A centrifugal pump is specified. Estimate the electrical power required by the pump, in \(\mathrm{kW}\). Is a centrifugal pump a good choice for this application? What precautions should be taken to avoid cavitation?

Air enters a compressor operating at steady state at \(17^{\circ} \mathrm{C}\), 1 bar and exits at a pressure of 5 bar. Kinetic and potential energy changes can be ignored. If there are no internal irreversibilities, evaluate the work and heat transfer, each in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of air flowing, for the following cases: (a) isothermal compression. (b) polytropic compression with \(n=1.3\). (c) adiabatic compression. Sketch the processes on \(p-v\) and \(T-s\) coordinates and associate areas on the diagrams with the work and heat transfer in each case. Referring to your sketches, compare for these cases the magnitudes of the work, heat transfer, and final temperatures, respectively.

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