/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 33 Carbon dioxide gas enters a well... [FREE SOLUTION] | 91Ó°ÊÓ

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Carbon dioxide gas enters a well-insulated diffuser at \(138 \mathrm{kPa}, 278 \mathrm{~K}\), with a velocity of \(244 \mathrm{~m} / \mathrm{s}\) through a flow area of \(9 \mathrm{~cm}^{2}\). At the exit, the flow area is 30 times the inlet area, and the velocity is \(6 \mathrm{~m} / \mathrm{s}\). The potential energy change from inlet to exit is negligible. For steady-state operation, determine the exit temperature, in \({ }^{\circ} \mathrm{K}\), the exit pressure, in \(\mathrm{kPa}\), and the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\).

Short Answer

Expert verified
Exit temperature: 248.9 K, Exit pressure: 138.9 kPa, Mass flow: 0.48 kg/s.

Step by step solution

01

- List Given Data

Write down all the given data: - Inlet pressure \(P_1 = 138 \text{kPa}\) - Inlet temperature \(T_1 = 278 \text{K}\)- Inlet velocity \(v_1 = 244 \text{m/s}\)- Inlet area \(A_1 = 9 \text{cm}^2 = 9 \times 10^{-4} \text{m}^2\)- Exit flow area \(A_2 = 30 \times A_1 = 0.027 \text{m}^2\)- Exit velocity \(v_2 = 6 \text{m/s}\)
02

- Apply Mass Flow Rate Equation

Use the mass flow equation \(\dot{m} = \rho v A\).We need to find \(\rho_1\):We can use the ideal gas relation: \[\rho = \frac{P}{{R_u / MW} \cdot T}\]Given, \(R_u = 8314 \text{J/(kmol}\cdot\text{K)}\)We find the molecular weight of CO2 \(MW = 44 \text{kg/kmol}\): \[\rho_1 = \frac{138 \text{kPa}}{{8314 \text{J/(kmol}\cdot\text{K)}} / 44 \text{kg/kmol}}\times 278 \text{K}\]Solve for \rho_1 and then \dot{m} using the inlet conditions.
03

- Calculate Density

Identify: \[\rho_1 = \frac{138 \text{kPa}}{{8314 \text{J/(kmol}\cdot\text{K)}} / 44 \text{kg/kmol}}\times 278 \text{K}\]Convert pressure to Pascals: \[138 \text{kPa} \rightarrow 138000 \text{Pa}\] Solve for \rho_1: \[\rho_1 = \frac{138000}{(8314/44)\times 278} \approx 2.176 \text{kg/m}^3\]
04

- Determine Mass Flow Rate

Use the mass flow rate equation: \[\dot{m} = \rho_1 v_1 A_1\]Calculate: \[\dot{m} = 2.176 \text{kg}/m^3 \times 244 \text{m}/s \times 9 \times 10^{-4} \text{m}^2 \approx 0.48 \text{kg}/s\]
05

- Apply Steady-State Energy Equation

Write down the steady-state energy equation:Assuming steady flow system with negligible potential energy changes and heat transfer: \[h_1 + \frac{v_1^2}{2} = h_2 + \frac{v_2^2}{2}\]Since \(h = c_p \cdot T \), find the exit temperature \(T_2\)
06

- Calculate Exit Temperature

Solve for \ T_2 \ using energy equation:Use the specific heat \(c_p \text{ for CO}_2 = 844 \text{J/(kg} \text{K)}\)Set up equation: \[c_p(T_1 - T_2) = \frac{v_1^2 - v_2^2}{2} \implies T_2 = T_1 - \frac{v_1^2 - v_2^2}{2c_p}\] Calculate the values to find \T_2: \[T_2 = 278 - \frac{244^2 - 6^2}{2 \cdot 844} \approx 248.9 \text{K}\]
07

- Apply Continuity and Ideal Gas Law for Exit Pressure

Use the continuity equation: \[\dot{m} = \rho_2 v_2 A_2\]Rearrange to find \rho_2:\[\rho_2 = \frac{\dot{m}}{v_2 A_2} \approx \frac{0.48 \text{kg/s}}{6 \text{m/s} \times 0.027 \text{m}^2} = 2.963 \text{kg/m}^3 \text{(approximately)}\]Use ideal gas law: Plug values into: \[P_2 = \rho_2 \cdot \frac{R_u}{MW} \cdot T_2 \implies P_2 = 2.963 \text{kg/m}^3 \times \frac{8314}{44} \cdot 248.9\]Convert result to \text{kPa}
08

- Calculate Exit Pressure

Calculate exit pressure: \[P_2 = 2.963 \text{kg/m}^3 \times \frac{8314}{44} \cdot 248.9 \approx 138.9 \text{kPa}\]

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Key Concepts

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

steady-state energy equation
In thermodynamics, the steady-state energy equation helps to analyze systems where conditions remain constant over time. This means that the energy entering the system equals the energy leaving it. For our diffuser problem, we consider kinetic and enthalpy changes since potential energy differences are negligible.

By writing the equation as: \[ h_1 + \frac{v_1^2}{2} = h_2 + \frac{v_2^2}{2} \] we are balancing the specific enthalpy and kinetic energy of the gas at the entry (subscript 1) and at the exit (subscript 2), with: \[ h = c_p \times T \] The specific heat capacity \( c_p \) is used to relate the temperature changes to the enthalpy. This equation gives us the tools to solve for the exit temperature when given the velocities and temperatures of the gas entering and exiting the diffuser.
mass flow rate
The mass flow rate \( \dot{m} \) is a measure of the amount of mass flowing through a cross-section of a stream per unit time. For our exercise, we use the equation: \( \dot{m} = \rho v A \), where \( \rho \) is the density, \( v \) is the velocity, and \( A \) is the flow area.

First, we calculate the density at the inlet using the ideal gas law. With density in hand, we determine the mass flow rate using the inlet conditions. This value, calculated once, applies to both the inlet and outlet due to conservation of mass in a steady-flow system.
ideal gas law
The ideal gas law links pressure \( P \), volume \( V \), temperature \( T \), and the amount of gas in moles \( n \). It is expressed as: \[ PV = nRT \] or in terms of density: \[ \rho = \frac{P}{\left( \frac{R_u}{MW} \right) T} \] Here, the universal gas constant \( R_u \) and the molecular weight \( MW \) of the gas are used to convert the pressure and temperature into density. This equation was critical in finding the densities needed for mass flow rate calculations and further analysis.
specific heat capacity
Specific heat capacity \( c_p \) is the amount of heat required to raise the temperature of one kilogram of a substance by one Kelvin. In our problem, it is used to transition between the temperatures and the enthalpies of the gas. For carbon dioxide, \( c_p \) is given as 844 J/(kg·K).
By applying this to our energy balance equation, we can solve for temperature changes: \[ c_p \left( T_1 - T_2 \right) = \frac{v_1^2 - v_2^2}{2} \]
continuity equation
The continuity equation states that the mass flow rate is the same at all points in a closed system. It is expressed as: \[ \dot{m} = \rho_1 v_1 A_1 = \rho_2 v_2 A_2 \] This equation asserts that the products of density, velocity, and cross-sectional area at the inlet and outlet remain equal because mass is conserved. Using the continuity equation, the densities at the exit can be derived from the calculated mass flow rates, incorporating the exit velocities and areas.

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Most popular questions from this chapter

Refrigerant \(134 \mathrm{a}\) enters a heat exchanger at \(-12^{\circ} \mathrm{C}\) and a quality of \(42 \%\) and exits as saturated vapor at the same temperature with a volumetric flow rate of \(0.85 \mathrm{~m}^{3} / \mathrm{min}\). A separate stream of air enters at \(22^{\circ} \mathrm{C}\) with a mass flow rate of \(188 \mathrm{~kg} / \mathrm{min}\) and exits at \(17^{\circ} \mathrm{C}\). Assuming the ideal gas model for air and ignoring kinetic and potential energy effects, determine (a) the mass flow rate of the Refrigerant \(134 \mathrm{a}\), in \(\mathrm{kg} / \mathrm{min}\), and (b) the heat transfer between the heat exchanger and its surroundings, in \(\mathrm{kJ} / \mathrm{min}\).

Refrigerant \(134 \mathrm{a}\) enters the condenser of a refrigeration system operating at steady state at \(9 \mathrm{bar}, 50^{\circ} \mathrm{C}\), through a 2.5-cm-diameter pipe. At the exit, the pressure is 9 bar, the temperature is \(30^{\circ} \mathrm{C}\), and the velocity is \(2.5 \mathrm{~m} / \mathrm{s}\). The mass flow rate of the entering refrigerant is \(6 \mathrm{~kg} / \mathrm{min}\). Determine (a) the velocity at the inlet, in \(\mathrm{m} / \mathrm{s}\). (b) the diameter of the exit pipe, in \(\mathrm{cm}\).

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 \(90 \mathrm{~kg} / \mathrm{min}\).

At steady state, a well-insulated compressor takes in air at \(15^{\circ} \mathrm{C}, 98 \mathrm{kPa}\), with a volumetric flow rate of \(0.57 \mathrm{~m}^{3} / \mathrm{s}\), and compresses it to \(260^{\circ} \mathrm{C}, 827 \mathrm{kPa}\). Kinetic and potential energy changes from inlet to exit can be neglected. Determine the compressor power, in \(\mathrm{kW}\), and the volumetric flow rate at the exit, in \(\mathrm{m}^{3} / \mathrm{s}\).

A \(0.75 \mathrm{~m}^{3}\) capacity tank contains a two-phase liquid-vapor mixture at \(240^{\circ} \mathrm{C}\) and a quality of \(0.6 .\) Heat is transferred to the mixture and saturated vapor from the tank are withdrawn at \(240^{\circ} \mathrm{C}\) to maintain the constant pressure inside the tank by means of a pressure regulating value. This process continues until the tank has only saturated vapor left in it. Neglect the effect of kinetic and potential energies. Determine the amount of heat transfer in \(\mathrm{kJ}\).

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