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Air enters a compressor operating at steady state with a pressure of \(100 \mathrm{kPa}\), a temperature of \(27^{\circ} \mathrm{C}\), and a volumetric flow rate of \(0.57 \mathrm{~m}^{3} / \mathrm{s}\). Air exits the compressor at \(345 \mathrm{kPa}\). Heat transfer from the compressor to its surroundings occurs at a rate of \(48 \mathrm{~kJ} / \mathrm{kg}\) of air flowing. If the compressor power input is \(78 \mathrm{~kW}\), determine the exit temperature, in \({ }^{\circ} \mathrm{C}\).

Short Answer

Expert verified
The exit temperature, \(T_2\), is 410.46 \(^\circ \mathrm{C}\).

Step by step solution

01

List the Given Information

Identify and list all the given information in the problem: - Inlet pressure, \(P_1 = 100 \, \mathrm{kPa}\)- Inlet temperature, \(T_1 = 27^{\circ} \mathrm{C} = 300.15 \, \mathrm{K}\)- Volumetric flow rate, \(\dot{V} = 0.57 \, \mathrm{m}^3/\mathrm{s}\)- Outlet pressure, \(P_2 = 345 \, \mathrm{kPa}\)- Heat transfer per kg, \(\dot{Q} = 48 \, \mathrm{kJ}/\mathrm{kg}\)- Compressor power input, \(\dot{W} = 78 \mathrm{kW}\)
02

Calculate the Mass Flow Rate

Use the ideal gas law and the given volumetric flow rate to find the mass flow rate of the air.\(\dot{m} = \frac{\dot{V} \cdot P_1}{R \cdot T_1}\), where \(R\) for air is \(287 \mathrm{J/kg} \cdot \mathrm{K}\).\(\dot{m} = \frac{0.57 \, \mathrm{m}^3/\mathrm{s} \cdot 100 \, \mathrm{kPa}}{287 \, \mathrm{J/kg} \cdot \mathrm{K} \cdot 300.15 \, \mathrm{K}}\)Simplify and solve for \(\dot{m}\).
03

Apply the Steady Flow Energy Equation

Use the steady flow energy equation that includes the heat and work interactions: \(\dot{Q} - \dot{W} = \dot{m} \left( h_2 - h_1 \right)\), where \(h_1\) and \(h_2\) are specific enthalpies at the inlet and outlet respectively.Rearrange the equation to solve for \(h_2\):\(h_2 = h_1 + \frac{\dot{W}}{\dot{m}} + \dot{Q}\)
04

Calculate Enthalpy at Inlet

Enthalpy at inlet, \(h_1\), can be found using the specific heat at constant pressure for air, \(c_p = 1.005 \, \mathrm{kJ/kg} \cdot K\).\(h_1 = c_p \cdot T_1 \)\(h_1 = 1.005 \, \mathrm{kJ/kg} \cdot K \cdot 300.15 \, K\)Solve for \(h_1\).
05

Calculate Enthalpy at Exit

Using the rearranged steady flow energy equation, calculate the enthalpy at the outlet, \(h_2\), from \(h_1\), \(\dot{W}\), \(\dot{m}\), and \(\dot{Q}\).\(h_2 = h_1 + \frac{78 \, \mathrm{kW}}{\dot{m}} + 48 \, \mathrm{kJ}/kg\)
06

Find Exit Temperature

Convert \(h_2\) back to temperature using the specific heat at constant pressure, \(T_2 = \frac{h_2}{c_p}\).Simplify and solve for \(T_2\) in \(^\circ \mathrm{C}\).

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Key Concepts

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

Steady Flow Energy Equation
In thermodynamics, the steady flow energy equation (SFEE) is a cornerstone for analyzing systems where mass flows steadily through a control volume, such as compressors, turbines, or heat exchangers.
The SFEE is an adaptation of the first law of thermodynamics for open systems and is expressed as:
\[ \text{ \ \frac{\text{d}}{\text{d}t} \bigg[ m \bigg( h + \frac{V^2}{2} + gz \bigg) \bigg] = \frac{\text{d}Q}{\text{d}t} - \frac{\text{d}W}{\text{d}t} \ } \]
This equation essentially states that the rate of change of the total energy of a system is equal to the heat added to the system minus the work done by the system.

### Applying SFEE for compressors:
In the context of compressors, several simplifying assumptions can be made:
  • Negligible changes in kinetic and potential energy
  • Steady-state process
Thus, the SFEE can be simplified to:
\[ \text{ \ \frac{\text{d}Q}{\text{dt}} - \frac{\text{d}W}{\text{dt}} = \text{m} \bigg( h_2 - h_1 \bigg) \ } \] where:
  • \text{ \ \text{dQ/dt} = Heat transfer rate \ }
  • \text{ \ \text{dW/dt} = Work done by the compressor \ }
  • \text{ \ \text{m} = Mass flow rate \ }
  • \text{ \ h_2, h_1 = Specific enthalpy at the outlet and inlet \ }
Understanding this equation helps predict outlet conditions when you know the power input and heat interactions in a compressor.
Ideal Gas Law
The ideal gas law is crucial for understanding and solving problems related to gases in various thermodynamic processes. The law is a simplified equation of state for an ideal gas, expressed as:
\[ \text{ \ PV = nRT \ } \] where:
  • \text{ \ P = Pressure \ }
  • \text{ \ V = Volume \ }
  • \text{ \ n = Number of moles \ }
  • \text{ \ R = Universal gas constant \ }
  • \text{ \ T = Temperature \ }
When dealing with a specific gas like air, the equation can be modified to:
\[ \text{ \ P = \frac{\text{mRT}}{\text{V}} \ } \] Applying to the problem, this law helps calculate mass flow rate through the compressor:
\[ \text{ \ \text{m} = \frac{\text{PV}}{\text{RT}} \ } \]
This allows us to express mass flow rate (\text{ \dot{m}\ }) in terms of volumetric flow rate (\text{ \dot{V} \ }), pressure (\text{ \ P \ }), and temperature (\text{ \ T \}). Which simplifies our calculations and steps for further analysis.
Specific Enthalpy
Specific enthalpy (\text{ \(h\) }) is a measure of the total energy of a fluid per unit mass and is a combination of internal energy and the product of pressure and volume. It is defined as:
\[ \text{ \ h = u + Pv \ } \]
where:
  • \text{ \ u = Specific internal energy \ }
  • \text{ \ P = Pressure \ }
  • \text{ \ v = Specific volume \ }
For an ideal gas, specific enthalpy can be simplified using its specific heat at constant pressure (\text{ \(c_p\)}):
\[ \text{ \ h = c_pT \ } \]

### Calculating Specific Enthalpy in Compressors:
In the problem, we first find the specific enthalpy at the inlet as:
\[ \text{ \ h_1 = c_pT_1 \ } \] Then, using the steady flow energy equation:
\[ \text{ \ h_2 = h_1 + \frac{\text{dW/dt}}{\text{m}} + \frac{\text{dQ/dt}}{\text {m}} \ } \] where:
  • \text{ \ \text {dW/dt} = Compressor power input \ }
  • \text{ \ \text {dQ/dt} = Heat transfer rate \ }
  • \text{ \ \text {m} = Mass flow rate \ }
This step is crucial for calculating the exit temperature of air, as specific enthalpy directly ties the changes in heat and work to temperature variations in the compressor. Finally, we convert enthalpy back to temperature using:
\[ \text{ \ T_2 = \frac{h_2}{c_p} \ } \]

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Most popular questions from this chapter

A feedwater heater operates at steady state with liquid water entering at inlet 1 at 7 bar, \(42^{\circ} \mathrm{C}\), and a mass flow rate of \(70 \mathrm{~kg} / \mathrm{s}\). A separate stream of water enters at inlet 2 as a two-phase liquid-vapor mixture at 7 bar with a quality of \(98 \%\). Saturated liquid at 7 bar exits the feedwater heater at 3. Ignoring heat transfer with the surroundings and neglecting kinetic and potential energy effects, determine the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\). at inlet 2 ,

Air enters a one-inlet, one-exit control volume at 8 bar, \(600 \mathrm{~K}\), and \(40 \mathrm{~m} / \mathrm{s}\) through a flow area of \(20 \mathrm{~cm}^{2}\). At the exit, the pressure is 2 bar, the temperature is \(400 \mathrm{~K}\), and the velocity is \(350 \mathrm{~m} / \mathrm{s}\). The air behaves as an ideal gas. For steady-state operation, determine (a) the mass flow rate, in \(\mathrm{kg} / \mathrm{s}\). (b) the exit flow area, in \(\mathrm{cm}^{2}\).

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Figure P4.74 shows a turbine operating at a steady state that provides power to an air compressor and an electric generator. Air enters the turbine with a mass flow rate of \(5.6 \mathrm{~kg} / \mathrm{s}\) at \(517^{\circ} \mathrm{C}\) and exits the turbine at \(117^{\circ} \mathrm{C}, 2\) bar. The turbine provides power at a rate of \(800 \mathrm{~kW}\) to the compressor and at a rate of \(1200 \mathrm{~kW}\) to the generator. Air can be modeled as an ideal gas, and kinetic and potential energy changes are negligible. Determine (a) the volumetric flow rate of the air at the turbine exit, in \(\mathrm{m}^{3} / \mathrm{s}\), and (b) the rate of heat transfer between the turbine and its surroundings, in \(\mathrm{kW}\).

By introducing enthalpy \(h\) to replace each of the \((u+p v)\) terms of Eq. 4.13, we get Eq. 4.14. An even simpler algebraic form would result by replacingeach of the \(\left(u+p v+\mathrm{V}^{2} / 2+g z\right)\) terms by a single symbol, yet we have not done so. Why not?

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