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Air enters a diffuser operating at steady state at \(540^{\circ} \mathrm{R}\), 15 lbf/in. \({ }^{2}\), with a velocity of \(600 \mathrm{ft} / \mathrm{s}\), and exits with a velocity of \(60 \mathrm{ft} / \mathrm{s}\). The ratio of the exit area to the inlet area is 8 . Assuming the ideal gas model for the air and ignoring heat transfer, determine the temperature, in \({ }^{\circ} \mathrm{R}\), and pressure, in lbf/in. \({ }^{2}\), at the exit.

Short Answer

Expert verified
P_2=540R ; R56 end

Step by step solution

01

Apply Continuity Equation

First, use the continuity equation for steady-state flow to relate the inlet and exit conditions:\[\begin{equation}\rho_1 V_1 A_1 = \rho_2 V_2 A_2ewline\rho_1 \frac{V_1}{V_2} = 8 \rho_2ewline\rho_1 = 8 \rho_2ewline\frac{\rho_2}{\rho_1} = \frac{1}{8}ewline\end{equation}\]This follows from the mass flow rate conservation, where the product of density (\( \rho \)), velocity (\( V \)), and area (\( A \)) remains constant.
02

Application Bernoulli sion

540-58

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Key Concepts

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

Continuity Equation
The continuity equation is essential in understanding fluid dynamics. It states that in a steady-state flow, the mass flow rate must remain constant from one cross-section of a pipe or duct to another.
This principle can be represented mathematically as: \[ \rho_1 V_1 A_1 = \rho_2 V_2 A_2 \]
Here, \( \rho \) is the fluid density, \( V \) is the flow velocity, and \( A \) is the cross-sectional area of the flow. In the problem, we see that the airflow enters and exits with different velocities and areas.
To maintain steady-state conditions, if the area increases eightfold, the exit density must decrease accordingly to balance the equation.
This concept ensures that mass is neither created nor destroyed in the system. Hence, we calculate the relation between the densities at the inlet and outlet.
Density
Density is a measure of mass per unit volume, and it plays a crucial role in the continuity equation. In the context of our problem, we need to consider how density changes as the air moves through the diffuser.
Since density is directly related to pressure and temperature for gases, understanding the variations helps us solve for the exit conditions.
Given that the inlet density \( \rho_1 \) is related to the exit density \( \rho_2 \) by: \[ \frac{\rho_2}{\rho_1} = \frac{1}{8} \]
This implies that if the area at the exit increases substantially as given, the density must decrease for the continuity equation to hold.
Velocity
Velocity is the speed at which the fluid particles move through a given point. It's inversely proportional to the area in the continuity equation.
In our exercise, the airflow velocity decreases from \( 600 \ \text{ft/s} \) to \( 60 \ \text{ft/s} \) as it exits the diffuser. This reduction aligns with the increase in the cross-sectional area by a factor of 8.
Velocity changes are pivotal as they impact both the kinetic energy and pressure. As airflow decelerates in the diffuser, there’s a corresponding increase in pressure energy, helping us solve the Bernoulli equation for the system.
Ideal Gas Model
The ideal gas model simplifies the relationships between pressure, volume, and temperature for gases. It is represented by the equation: \[ PV = nRT \]
For the exercise, the ideal gas law helps us relate the temperature and pressure changes between the inlet and outlet.
Using it, we can determine the temperature at the exit given the conditions at the entrance and the changes in density and pressure as calculated using the continuity and Bernoulli equations.
Bernoulli Equation
The Bernoulli equation for fluid flow combines principles of energy conservation. It balances the kinetic energy, potential energy, and internal energy within a fluid system: \[ P + \frac{1}{2} \rho V^2 + \rho gh = \text{constant} \]
Ignoring elevation changes (g and h), the equation primarily relates pressure and velocity changes.
In solving the exercise, applying the Bernoulli equation helps us determine the pressure drop or increase due to the velocity reduction. Given the problems' numbers, we utilize the known values to compute the exit temperature and pressure, ensuring the equations align under the steady-state assumption without heat transfer.

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Most popular questions from this chapter

Figure P4.101 shows a pumped-hydro energy storage system delivering water at steady state from a lower reservoir to an upper reservoir using off-peak electricity (see Sec. 4.8.3). Water is delivered to the upper reservoir at a volumetric flow rate of \(150 \mathrm{~m}^{3} / \mathrm{s}\) with an increase in elevation of \(20 \mathrm{~m}\). There is no significant change in temperature, pressure, or kinetic energy from inlet to exit. Heat transfer from the pump to its surroundings occurs at a rate of \(0.6 \mathrm{MW}\) and \(g=9.81 \mathrm{~m} / \mathrm{s}^{2}\). Determine the pump power required, in MW. Assuming the same volumetric flow rate when the system generates on-peak electricity using this water, will the power be greater, less, or the same as the pump power? Explain.

An open feedwater heater operates at steady state with liquid water entering inlet 1 at 10 bar, \(50^{\circ} \mathrm{C}\), and a mass flow rate of \(60 \mathrm{~kg} / \mathrm{s}\). A separate stream of steam enters inlet 2 at 10 bar and \(200^{\circ} \mathrm{C}\). Saturated liquid at 10 bar exits the feedwater heater at exit 3 . Ignoring heat transfer with the surroundings and neglecting kinetic and potential energy effects, determine the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\), of the steam at inlet 2 .

Steam enters a heat exchanger operating at steady state at \(250 \mathrm{kPa}\) and a quality of \(90 \%\) and exits as saturated liquid at the same pressure. A separate stream of oil with a mass flow rate of \(29 \mathrm{~kg} / \mathrm{s}\) enters at \(20^{\circ} \mathrm{C}\) and exits at \(100^{\circ} \mathrm{C}\) with no significant change in pressure. The specific heat of the oil is \(c=2.0 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\). Kinetic and potential energy effects are negligible. If heat transfer from the heat exchanger to its surroundings is \(10 \%\) of the energy required to increase the temperature of the oil, determine the steam mass flow rate, in \(\mathrm{kg} / \mathrm{s}\).

Air enters a horizontal, constant-diameter heating duct operating at steady state at \(290 \mathrm{~K}, 1\) bar, with a volumetric flow rate of \(0.25 \mathrm{~m}^{3} / \mathrm{s}\), and exits at \(325 \mathrm{~K}, 0.95\) bar. The flow area is \(0.04 \mathrm{~m}^{2}\). Assuming the ideal gas model with \(k=1.4\) for the air, determine (a) the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\), (b) the velocity at the inlet and exit, each in \(\mathrm{m} / \mathrm{s}\), and (c) the rate of heat transfer, in \(\mathrm{kW}\).

Refrigerant \(134 a\) enters the evaporator of a refrigeration system operating at steady state at \(-4^{\circ} \mathrm{C}\) and quality of \(20 \%\) at a velocity of \(7 \mathrm{~m} / \mathrm{s}\). At the exit, the refrigerant is a saturated vapor at a temperature of \(-4^{\circ} \mathrm{C}\). The evaporator flow channel has constant diameter. If the mass flow rate of the entering refrigerant is \(0.1 \mathrm{~kg} / \mathrm{s}\), determine (a) the diameter of the evaporator flow channel, in \(\mathrm{cm}\). (b) the velocity at the exit, in \(\mathrm{m} / \mathrm{s}\).

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