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Air enters a compressor operating at steady state with a pressure of 1 bar, a temperature of \(20^{\circ} \mathrm{C}\), and a volumetric flow rate of \(0.25 \mathrm{~m}^{3} / \mathrm{s}\). The air velocity in the exit pipe is \(210 \mathrm{~m} / \mathrm{s}\) and the exit pressure is \(1 \mathrm{MPa}\). If each unit mass of air passing from inlet to exit undergoes a process described by \(p v^{1.34}=\) constant, determine the exit temperature, in \({ }^{\circ} \mathrm{C}\).

Short Answer

Expert verified
368.31 \( ^{\circ} \text{C} \)

Step by step solution

01

Identify given values

The problem gives the following values: - Inlet pressure, \( p_1 = 1 \text{ bar} \)- Inlet temperature, \( T_1 = 20^{\text{C}} = 293.15 \, \text{K} \)- Inlet volumetric flow rate, \( \dot{V}_1 = 0.25 \text{ m}^3\text{/s} \)- Exit velocity, \( v_2 = 210 \text{ m/s} \)- Exit pressure, \( p_2 = 1 \text{ MPa} = 1000 \text{ kPa} \)- Polytropic process exponent, \( n = 1.34 \)- Relation equation: \( p v^{1.34}=k \)
02

Express the inlet specific volume

Using the ideal gas law, the specific volume at the inlet can be expressed as \[ v_1 = \frac{RT_1}{p_1} \]where - R (specific gas constant for air) = 0.287 \text{ kJ/kg⋅K}- \( p_1 \) = 1 bar = 100 kPa- \( T_1 \) = 293.15 K Thus, \[ v_1 = \frac{0.287 \times 293.15}{100} = 0.841\text{m}^3/\text{kg} \]
03

Use the given polytropic process relation

Knowing the process is described by \( p v^{1.34} = k \), and given the inlet condition \( k = p_1 v_1^{1.34} \), we can write \[ k = 100 \times (0.841)^{1.34} \]Solving for k, \[ k = 76.96 \text{kPa⋅m}^{1.34/\text{kg}} \]
04

Calculate the exit specific volume

Rearranging the polytropic relation for exit conditions (i.e., \( p_2 v_2^{1.34} = k \)) gives \[ v_2 = \left(\frac{k}{p_2}\right)^{\frac{1}{1.34}}\]Substituting the known values, \[ v_2 = \left(\frac{76.96}{1000}\right)^{\frac{1}{1.34}} = 0.184 \text{m}^3/\text{kg} \]
05

Calculate mass flow rate using inlet conditions

The mass flow rate at the inlet can be determined by \[ \dot{m} = \frac{\dot{V}_1}{v_1} \] Substituting known values, \[ \dot{m} = \frac{0.25}{0.841} = 0.297 \text{ kg/s} \]
06

Determine the exit temperature

Use the ideal gas law again to find the exit temperature: \[ T_2 = \frac{p_2 v_2}{R} \] Substituting in the known values, \[ T_2 = \frac{1000 \times 0.184}{0.287} = 641.46 \text{ K} \] Converting to Celsius, \[ T_2 = 641.46 - 273.15 = 368.31 ^{\circ} \text{C} \]

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Key Concepts

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

Polytropic Processes
A polytropic process is a type of thermodynamic process that typically occurs in various industrial devices like compressors and turbines. It’s characterized by the equation:
\[ pv^n = k \]
Here, p stands for pressure, v is specific volume, n is the polytropic index, and k is a constant. This equation shows how pressure and specific volume are related during the process.
Different values of n describe different processes:
  • n = 1 corresponds to an isothermal process (constant temperature).
  • n = γ (where \( \gamma = \frac{C_p}{C_v} \) ) describes an adiabatic process (no heat exchange).

In this exercise, the process follows a polytropic index of 1.34, which is typical for many real-world applications. Understanding this equation helps us predict how gas properties will change during compression or expansion.
Ideal Gas Law
The Ideal Gas Law is a fundamental equation in thermodynamics that relates pressure, volume, and temperature of an ideal gas. It is represented as:
\[ PV = nRT \]
Here:
  • P - Pressure
  • V - Volume
  • n - Number of moles
  • R - Universal gas constant
  • T - Temperature

For calculations involving specific volume (volume per unit mass), the equation takes the form:
\[ v = \frac{RT}{P} \]
Where, v is the specific volume, R is the specific gas constant, and P and T are the given pressure and temperature respectively. This law is a key tool in determining properties like specific volume and temperature at different stages in thermodynamic cycles, making it crucial for solving the exercise.
Mass Flow Rate Calculation
The mass flow rate is a measure of the mass of a substance passing through a given surface per unit time. It’s essential for analyzing systems involving fluid flow, such as compressors. For incompressible or ideal gas conditions, it is calculated as:
\[ \dot{m} = \frac{\dot{V}_1}{v_1} \]
Where:
  • \dot{m} - Mass flow rate
  • \dot{V}_1 - Volumetric flow rate
  • v_1 - Specific volume at the inlet

Knowing the mass flow rate helps in further calculations and ensures energy balance across the system. In this exercise, we determine it to understand the rate at which air is moving through the compressor under given conditions.
Specific Volume
Specific volume is an intrinsic property of a substance, defined as the volume occupied by a unit mass. It is the reciprocal of density and plays a vital role in thermodynamic calculations. For ideal gases, it can be calculated using the Ideal Gas Law:
\[ v = \frac{RT}{P} \]
Here, v is the specific volume, R is the specific gas constant, and P and T are the given pressure and temperature.
For the inlet conditions in our problem, we used this formula to find the specific volume of air, which was essential for subsequent steps such as calculating the mass flow rate and applying the polytropic process equation.

Understanding specific volume helps visualize how the same mass of a gas takes up different volumes under varying pressure and temperature conditions.
Exit Temperature Calculation
One of the final steps in analyzing a thermodynamic process like in this exercise is determining the exit temperature of the gas. For this purpose, we use the Ideal Gas Law rearranged to solve for temperature:
\[ T_2 = \frac{p_2v_2}{R}\]
Here:
  • p_2 - Exit pressure
  • v_2 - Exit specific volume
  • R - Specific gas constant

Substituting in the known values provides the exit temperature in Kelvin, which can be further converted to Celsius if needed.
This calculation ensures we understand the thermal effects of the compression process, crucial for designing efficient compressor systems and predicting performance under various operating conditions.

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Most popular questions from this chapter

Sensibly Built Homes Cost No More (see box Sec. 4.3). In energy-efficient homes, indoor air quality can be a concern. Research the issue of carbon monoxide and radon buildup in tightly sealed houses. Write a report including at least three references.

Air enters a water-jacketed air compressor operating at steady state with a volumetric flow rate of \(37 \mathrm{~m}^{3} / \mathrm{min}\) at 136 \(\mathrm{kPa}, 305 \mathrm{~K}\) and exits with a pressure of \(680 \mathrm{kPa}\) and a temperature of \(400 \mathrm{~K}\). The power input to the compressor is \(155 \mathrm{~kW}\). Energy transfer by heat from the compressed air to the cooling water circulating in the water jacket results in an increase in the temperature of the cooling water from inlet to exit with no change in pressure. Heat transfer from the outside of the jacket as well as all kinetic and potential energy effects can be neglected. (a) Determine the temperature increase of the cooling water, in \(\mathrm{K}\), if the cooling water mass flow rate is \(82 \mathrm{~kg} / \mathrm{min}\). (b) Plot the temperature increase of the cooling water, in \(\mathrm{K}\), versus the cooling water mass flow rate ranging from 75 to \(90 \mathrm{~kg} / \mathrm{min}\).

Vegetable oil for cooking is dispensed from a cylindrical can fitted with a spray nozzle. According to the label, the can is able to deliver 560 sprays, each of duration \(0.25 \mathrm{~s}\) and each having a mass of \(0.25 \mathrm{~g}\). Determine (a) the mass flow rate of each spray, in \(\mathrm{g} / \mathrm{s}\). (b) the mass remaining in the can after 560 sprays, in \(\mathrm{g}\), if the initial mass in the can is \(170 \mathrm{~g}\).

An oil pump operating at steady state delivers oil at a rate of \(5.5 \mathrm{~kg} / \mathrm{s}\) and a velocity of \(6.8 \mathrm{~m} / \mathrm{s}\). The oil, which can be modeled as incompressible, has a density of \(1600 \mathrm{~kg} / \mathrm{m}^{3}\) and experiences a pressure rise from inlet to exit of \(28 \mathrm{Mpa}\). There is no significant elevation difference between inlet and exit, and the inlet kinetic energy is negligible. Heat transfer between the pump and its surroundings is negligible, and there is no significant change in temperature as the oil passes through the pump. If pumps are available in \(1 / 4\)-horsepower increments, determine the horsepower rating of the pump needed for this application.

The air supply to a \(56 \mathrm{~m}^{3}\) office has been shut off overnight to conserve utilities, and the room temperature has dropped to \(4^{\circ} \mathrm{C}\). In the morning, a worker resets the thermostat to \(21^{\circ} \mathrm{C}\), and \(6 \mathrm{~m}^{3} / \mathrm{min}\) of air at \(50^{\circ} \mathrm{C}\) begins to flow in through a supply duct. The air is well mixed within the room, and an equal mass flow of air at room temperature is withdrawn through a return duct. The air pressure is nearly 1 bar everywhere. Ignoring heat transfer with the surroundings and kinetic and potential energy effects, estimate how long it takes for the room temperature to reach \(21^{\circ} \mathrm{C}\). Plot the room temperature as a function of time.

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