/*! 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 56 Carbon dioxide gas is compressed... [FREE SOLUTION] | 91Ó°ÊÓ

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Carbon dioxide gas is compressed at steady state from a pressure of \(20 \mathrm{lbf} /\) in. \({ }^{2}\) and a temperature of \(32^{\circ} \mathrm{F}\) to a pressure of \(50 \mathrm{lbf} / \mathrm{in}^{2}\) and a temperature of \(120^{\circ} \mathrm{F}\). The gas enters the compressor with a velocity of \(30 \mathrm{ft} / \mathrm{s}\) and exits with a velocity of \(80 \mathrm{ft} / \mathrm{s}\). The mass flow rate is \(0.98 \mathrm{lb} / \mathrm{s}\). The magnitude of the heat transfer rate from the compressor to its surroundings is \(5 \%\) of the compressor power input. Using the ideal gas model with \(c_{p}=0.21 \mathrm{Btu} / \mathrm{bb} \cdot{ }^{\circ} \mathrm{R}\) and neglecting potential energy effects, determine the compressor power input, in horsepower.

Short Answer

Expert verified
16.08 horsepower

Step by step solution

01

- Convert Units

Convert all given temperatures to Rankine. Use the formula: \(T(°R) = T(°F) + 459.67\).So, the inlet temperature is \(T_1 = 32 + 459.67 = 491.67 \text{ °R}\).The outlet temperature is \(T_2 = 120 + 459.67 = 579.67 \text{ °R}\).
02

- Apply the First Law of Thermodynamics

Using the First Law of Thermodynamics for a control volume in steady state, neglecting potential energy effects: \[ \frac{\text{d} E_{\text{cv}}}{\text{d}t} = \frac{\text{d} m}{\text{d}t} (h_2 + \frac{V_2^2}{2} + gz_2 - h_1 - \frac{V_1^2}{2} - gz_1) + \text{Q}_{\text{in}} - \text{W}_{\text{cv}} = 0 \]Simplify to: \[ \text{W}_{\text{cv}} = \text{m} (h_2 - h_1) + \frac{\text{m}}{2}(V_2^2 - V_1^2) + \text{Q}_{\text{in}} \]
03

- Determine Enthalpy Change

For an ideal gas, the enthalpy change can be determined using the specific heat capacity at constant pressure: \[ \text{h}_2 - \text{h}_1 = \text{c}_p (T_2 - T_1) \]Given: \(T_1 = 491.67 \text{ °R}\), \(T_2 = 579.67 \text{ °R}\), and \(\text{c}_p = 0.21 \text{ Btu/lb·°R}\) So, \( \text{h}_2 - \text{h}_1 = 0.21 \times (579.67 - 491.67) = 0.21 \times 88 = 18.48 \text{ Btu/lb}\)
04

- Calculate Kinetic Energy Difference

Use the velocities to find the difference in kinetic energy: \[ \frac{V_2^2}{2} - \frac{V_1^2}{2} = \frac{80^2}{2} - \frac{30^2}{2} = 3200 - 450 = 2750 \text{(ft^2/s^2)} \]Convert to consistent units where \(1 \text{ Btu} = 778.17 \text{ ft-lb} \), so \( \frac{2750 \text{ ft}^2/\text{s}^2}{778.17 \text{ ft-lb/Btu}} ≈ 3.53 \text{ Btu/lb} \)
05

- Determine Heat Transfer

The heat transfer rate is given as 5% of the compressor power input. Using a heat transfer rate of \( \text{Q} = 0.05 \times \text{W} \).Therefore, \[ \text{W}_{\text{input}} = \frac{1}{0.95} (\text{W}_{\text{cv}}) \]
06

- Plug in Known Values and Solve for Power Input

Now, substitute the known values into the equation: \[ \text{W}_{\text{cv}} = \text{m}(\text{h}_2 - \text{h}_1 + \frac{V_2^2}{2} - \frac{V_1^2}{2}) = 0.98 \text{ lb/s} \times (18.48 \text{ Btu/lb} + 3.53 \text{ Btu/lb}) = 0.98 \times 22.01 \text{ Btu/s} = 21.57 \text{ Btu/s} \]Convert to horsepower: \[ 1 \text{ Btu/s} = 0.7079 \text{ hp} \]So, \[ 21.57 \times 0.7079 = 15.28 \text{ hp} \]Now, considering the heat loss: \[ \text{W}_{\text{input}} = \frac{15.28}{0.95} \text{ hp} ≈ 16.08 \text{ hp} \]

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Key Concepts

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

steady state compression
Steady state compression refers to a process where the conditions (such as pressure, temperature, and mass flow rate) at the inlet and outlet of the compressor remain constant over time. This simplifies the analysis because the energy changes can be measured consistently. In our exercise, carbon dioxide gas is compressed steadily from a lower to a higher pressure and temperature, with specific velocities at the entry and exit points. Steady state ensures that while the gas properties change during compression, they do so predictably and can be accounted for using established thermodynamic principles.
First Law of Thermodynamics
The First Law of Thermodynamics, often referred to as the Law of Energy Conservation, states that energy cannot be created or destroyed, only transformed. For a control volume like a compressor, this can be expressed in the form of an energy balance:
\[ \dot{Q} - \dot{W} = \dot{m} \left( h_2 + \frac{V_2^2}{2} - h_1 - \frac{V_1^2}{2} \right) \]
  • \(\dot{Q}\): Heat transfer rate
  • \(\dot{W}\): Work done by the compressor
  • \(\dot{m}\): Mass flow rate
  • \(h_1, h_2\): Enthalpy at the inlet and outlet
  • \(V_1, V_2\): Velocity at the inlet and outlet

In our problem, we adapt this equation to neglect potential energy changes since they are minimal compared to other energy terms. By analyzing the work done and heat transfer, we can calculate the compressor's power input accurately.
ideal gas
An ideal gas is a theoretical gas that adheres perfectly to the ideal gas law (PV = nRT). In this model, gas molecules do not interact with each other, and their individual volume is negligible compared to the container's volume.
  • PV: Pressure (P) times volume (V)
  • nRT: Number of moles (n) times the gas constant (R) and temperature (T)

In our exercise, carbon dioxide is treated as an ideal gas, meaning we can use simple gas laws and properties (like specific heat capacity at constant pressure, \(c_p\)) to determine other thermodynamic properties, such as enthalpy and temperature relationships.
enthalpy change
Enthalpy (denoted as \(H\)) is a measure of the total energy of a thermodynamic system, including internal energy and the product of pressure and volume. The change in enthalpy (\(\Delta H\)) for an ideal gas during a compression process can be calculated as:
\[ \Delta H = c_p \Delta T \]
This simplifies to:
  • \(c_p\): Specific heat capacity at constant pressure
  • \(\Delta T\): Temperature change

In our exercise, this means we can determine the change in enthalpy of the carbon dioxide gas as it compresses from the initial to the final state, using the provided specific heat capacity and temperature values.
kinetic energy
Kinetic energy (KE) is the energy possessed by a body due to its motion and is given by the formula: \[ KE = \frac{1}{2}mv^2 \]
In a compressor, the difference in kinetic energy between the inlet and outlet states must be accounted for. The change in kinetic energy (\(\Delta KE\)) is:
\[ \Delta KE = \frac{1}{2}m(V_2^2 - V_1^2) \]
  • m: Mass flow rate
  • V_1: Velocity at the inlet
  • V_2: Velocity at the outlet

In the given problem, the velocity change from the entry to exit significantly contributes to the total energy change. By converting these differences into consistent energy units, we can incorporate them into the overall energy balance to find the compressor's power input.

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Most popular questions from this chapter

Liquid water flows isothermally at \(20^{\circ} \mathrm{C}\) through a oneinlet, one-exit duct operating at steady state. The duct's inlet and exit diameters are \(0.02 \mathrm{~m}\) and \(0.04 \mathrm{~m}\), respectively. At the inlet, the velocity is \(40 \mathrm{~m} / \mathrm{s}\) and pressure is 1 bar. At the exit, determine the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\), and velocity, in \(\mathrm{m} / \mathrm{s}\).

A rigid copper tank, initially containing \(1 \mathrm{~m}^{3}\) of air at \(295 \mathrm{~K}, 5\) bar, is connected by a valve to a large supply line carrying air at \(295 \mathrm{~K}, 15\) bar. The valve is opened only as long as required to fill the tank with air to a pressure of 15 bar. Finally, the air in the tank is at \(310 \mathrm{~K}\). The copper tank, which has a mass of \(20 \mathrm{~kg}\), is at the same temperature as the air in the tank, initially and finally. The specific heat of the copper is \(c=0.385 \mathrm{~kJ} / \mathrm{kg} \cdot \mathrm{K}\). Assuming ideal gas behavior for the air, determine (a) the initial and final mass of air within the tank, each in \(\mathrm{kg}\), and (b) the heat transfer to the surroundings from the tank and its contents, in kJ, ignoring kinetic and potential energy effects.

A rigid tank whose volume is \(10 \mathrm{~L}\) is initially evacuated. A pinhole develops in the wall, and air from the surroundings at 1 bar, \(25^{\circ} \mathrm{C}\) enters until the pressure in the tank becomes 1 bar. No significant heat transfer between the contents of the tank and the surroundings occurs. Assuming the ideal gas model with \(k=1.4\) for the air, determine (a) the final temperature in the tank, in \({ }^{\circ} \mathrm{C}\), and (b) the amount of air that leaks into the tank, in \(g\).

Air enters a compressor operating at steady state at \(14.7\) \(\mathrm{lbf} / \mathrm{in} .^{2}\) and \(60^{\circ} \mathrm{F}\) and is compressed to a pressure of \(150 \mathrm{lbf} / / \mathrm{in} .^{2}\) As the air passes through the compressor, it is cooled at a rate of 10 Btu per lb of air flowing by water circulated through the compressor casing. The volumetric flow rate of the air at the inlet is \(5000 \mathrm{ft}^{3} / \mathrm{min}\), and the power input to the compressor is 700 hp. The air behaves as an ideal gas, there is no stray heat transfer, and kinetic and potential effects are negligible. Determine (a) the mass flow rate of the air, lb/s, and (b) the temperature of the air at the compressor exit, in \({ }^{\circ} \mathrm{F}\).

Steam with a quality of \(0.7\), pressure of \(1.5\) bar, and flow rate of \(10 \mathrm{~kg} / \mathrm{s}\) enters a steam separator operating at steady state. Saturated vapor at \(1.5\) bar exits the separator at state 2 at a rate of \(6.9 \mathrm{~kg} / \mathrm{s}\) while saturated liquid at \(1.5\) bar exits the separator at state 3 . Neglecting kinetic and potential energy effects, determine the rate of heat transfer, in \(\mathrm{kW}\), and its associated direction.

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