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Carbon monoxide enters a nozzle operating at steady state at \(5 \mathrm{bar}, 200^{\circ} \mathrm{C}, 1 \mathrm{~m} / \mathrm{s}\) and undergoes a polytropic expansion to 1 bar with \(n=1.2\). Using the ideal gas model and ignoring potential energy effects, determine (a) the exit velocity, in \(\mathrm{m} / \mathrm{s}\). (b) the rate of heat transfer between the gas and its surroundings, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of gas flowing.

Short Answer

Expert verified
The exit velocity is approximately 533.19 m/s. The rate of heat transfer is approximately zero kJ per kg.

Step by step solution

01

Identify the known parameters

Identify and list all the given parameters. Initial pressure, \(P_1 = 5 \text{ bar} = 500 \text{ kPa}\)Initial temperature, \(T_1 = 200^{\circ} \text{C} = 473 \text{ K}\)Initial velocity, \(V_1 = 1 \text{ m/s}\)Final pressure, \(P_2 = 1 \text{ bar} = 100 \text{ kPa}\)Polytropic index, \(n = 1.2\)
02

Apply the polytropic process equation

Use the polytropic process equation to find the final temperature. The equation is \[ P_{1}V_{1}^{n} = P_{2}V_{2}^{n} \] Since \(V \propto \frac{T}{P}\), we can rewrite the equation as: \[ \frac{T_{1}}{P_{1}^{(1-1/n)}} = \frac{T_{2}}{P_{2}^{(1-1/n)}} \] Solve for \( T_{2} \): \[ T_{2} = T_{1}\left(\frac{P_{2}}{P_{1}}\right)^{(1-1/n)} = 473\left(\frac{100}{500}\right)^{(1-1/1.2)} = 335.68 \text{ K} \]
03

Use the energy balance equation

Apply the energy balance equation for a control volume (nozzle) with no potential energy effects and steady state conditions. The equation is: \[ h_{1} + \frac{V_{1}^{2}}{2} = h_{2} + \frac{V_{2}^{2}}{2} + q \]Using \[ h = C_{P}T \], write the equation as: \[ C_{P}T_{1} + \frac{V_{1}^{2}}{2} = C_{P}T_{2} + \frac{V_{2}^{2}}{2} + q \]
04

Calculate the specific heat capacity

For carbon monoxide, assume \(C_{P} \approx 1.034 \text{ kJ/kg}\text{ยท} \text{K}\)
05

Compute the exit velocity

Subtract the enthalpy terms on both sides to isolate \( V_{2} \). That gives: \[ V_2 = \sqrt{ 2(C_P(T_1 - T_2)) + V_1^2 } \]Plugging in the values: \[ V_2 = \sqrt{ 2(1.034 \times 10^3 \times (473 - 335.68)) + 1^2 } \= \sqrt{ 2(1.034 \times 10^3 \times 137.32) + 1 } \= \sqrt{ 284,196 + 1 } = 533.19 \text{ m/s} \]
06

Calculate the rate of heat transfer

Make use of the energy balance equation: \[ h_{1} + \frac{V_{1}^{2}}{2} = h_{2} + \frac{V_{2}^{2}}{2} + q \]Rearrange the equation to solve for \ q : \[ q = C_P T_1 + \frac{V_1^2}{2} - C_P T_2 - \frac{V_2^2}{2} \= 1,000 \approx 0 \text{kJ/kg} . \]

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Key Concepts

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

steady state conditions
In thermodynamics, steady state conditions imply that properties within the system do not change over time, despite mass or energy crossing its boundaries. Everything entering or leaving has a balance. This helps make the equations simpler. For the nozzle problem, it means all entries and exits of mass and energy are constant over time.
  • The nozzle operates consistently without changing its internal state.
  • The entering and exiting mass flow rates are equal.
  • The heat transfer rate is constant.
Assuming steady state helps simplify the energy balance equation. This is because we don't need to account for changes over time. So, it lets us focus on the energy transformations occurring from inlet to outlet.
ideal gas model
The ideal gas model is a mathematical approximation that simplifies the behavior of gases. It relies on the ideal gas law: \[ PV = nRT \] where P is pressure, V is volume, n is the amount of substance (moles), R is the ideal gas constant, and T is temperature. This model assumes:
  • Gases consist of many tiny particles moving randomly.
  • Intermolecular forces are negligible.
  • The volume of individual molecules is minuscule compared to the total volume of gas.
In the nozzle problem, carbon monoxide (CO) is treated as an ideal gas. This means we can use simplified relationships between pressure, volume, and temperature, which makes solving the problem easier. Using the ideal gas law lets us deduce that: \[ V \propto \frac{T}{P} \]This relationship helps in deriving final temperatures and exit velocities using the polytropic process equations.
energy balance equation
The energy balance equation in thermodynamics is a statement of the conservation of energy. It says energy entering a system equals energy leaving it, plus any stored energy changes. For a steady state process with negligible potential energy change, it takes the form:\[ h_{1} + \frac{V_{1}^{2}}{2} = h_{2} + \frac{V_{2}^{2}}{2} + q \]where:
  • \(h_1, h_2\) are the specific enthalpies at the inlet and outlet,
  • \(V_1, V_2\) are the velocities at the inlet and outlet, and
  • \(q\)
  • is the specific heat transfer.
Specific enthalpy (h) is related to temperature (T) through the specific heat capacity at constant pressure (\(C_P\)):\[ h = C_P T \]In the nozzle exercise, the energy balance equation helps determine the exit velocity and rate of heat transfer. Calculating these relies on known states of the gas and its flow, allowing us to find unknowns like exit velocity and heat transfer.

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Most popular questions from this chapter

One-tenth kilogram of water executes a Carnot power cycle. At the beginning of the isothermal expansion, the water is a saturated liquid at \(160^{\circ} \mathrm{C}\). The isothermal expansion continues until the quality is \(98 \%\). The temperature at the conclusion of the adiabatic expansion is \(20^{\circ} \mathrm{C}\). (a) Sketch the cycle on \(T-s\) and \(p-v\) coordinates. (b) Determine the heat added and net work, each in kJ. (c) Evaluate the thermal efficiency.

Answer the following true or false. If false, explain why. (a) The change of entropy of a closed system is the same for every process between two specified states. (b) The entropy of a fixed amount of an ideal gas increases in every isothermal compression. (c) The specific internal energy and enthalpy of an ideal gas are each functions of temperature alone but its specific entropy depends on two independent intensive properties. (d) One of the \(T d s\) equations has the form \(T d s=d u-p d v\). (e) The entropy of a fixed amount of an incompressible substance increases in every process in which temperature decreases.

A closed system undergoes a process in which work is done on the system and the heat transfer \(Q\) occurs only at temperature \(T_{\mathrm{b}}\). For each case, determine whether the entropy change of the system is positive, negative, zero, or indeterminate. (a) internally reversible process, \(Q>0\). (b) internally reversible process, \(Q=0\). (c) internally reversible process, \(Q<0\). (d) internal irreversibilities present, \(Q>0\). (e) internal irreversibilities present, \(Q=0\). (f) internal irreversibilities present, \(Q<0\).

At steady state, a device receives a stream of saturated water vapor at \(210^{\circ} \mathrm{C}\) and discharges a condensate stream at \(20^{\circ} \mathrm{C}, 0.1 \mathrm{MPa}\) while delivering energy by heat transfer at \(300^{\circ} \mathrm{C}\). The only other energy transfer involves heat transfer at \(20^{\circ} \mathrm{C}\) to the surroundings. Kinetic and potential energy changes are negligible. What is the maximum theoretical amount of energy, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of steam entering, that could be delivered at \(300^{\circ} \mathrm{C} ?\)

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,

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