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Liquid water at \(20 \mathrm{lbf} / \mathrm{in}^{2}, 50^{\circ} \mathrm{F}\) enters a mixing chamber operating at steady state with a mass flow rate of \(5 \mathrm{lb} / \mathrm{s}\) and mixes with a separate stream of steam entering at \(20 \mathrm{lb} / / \mathrm{in} .{ }^{2}\), \(250^{\circ} \mathrm{F}\) with a mass flow rate of \(0.38 \mathrm{lb} / \mathrm{s}\) A single mixed stream exits at \(20 \mathrm{lbf} / \mathrm{in}^{2}, 130^{\circ} \mathrm{F}\). Heat transfer from the mixing chamber occurs to its surroundings. Neglect the effects of motion and gravity and let \(T_{0}=70^{\circ} \mathrm{F}, p_{0}=1 \mathrm{~atm}\). Determine the rate of exergy destruction, in Btu/s, for a control volume including the mixing chamber and enough of its immediate surroundings that heat transfer occurs at \(70^{\circ} \mathrm{F}\).

Short Answer

Expert verified
Exergy destruction rate is found by applying the exergy balance equation using the specific exergies and mass flow rates.

Step by step solution

01

- Define the exergy balance equation

The exergy balance for a control volume can be expressed as \[ \dot{E}_{\text{in}} - \dot{E}_{\text{out}} - \dot{E}_{\text{out,heat}} = \dot{E}_{\text{destroy}} \] where \( \dot{E}_{\text{in}} \) and \( \dot{E}_{\text{out}} \) are the flow exergies in and out of the control volume and \(\dot{E}_{\text{out,heat}}\) is the exergy associated with heat transfer.
02

- Calculate the flow exergies

To calculate the flow exergies, we need specific exergy values which are calculated as: \[ \psi =(h - h_0) - T_0(s - s_0) \] where \(h\) and \(s\) are the specific enthalpy and entropy, and \(h_0\) and \(s_0\) are the reference state specific enthalpy and entropy.
03

- Determine specific exergies at inlet and outlet

Using steam tables or Mollier diagrams, determine the specific enthalpy and entropy for liquid water at \(\ 20 \, \mathrm{lbf}/\mathrm{in}^2\) , \( 50^\text{o}\text{F} \) and steam at \( \ 20 \, \mathrm{lbf}/\mathrm{in}^2\),\( 250^\text{o}\text{F}\) , as well as the mixed stream at \(\ 20 \, \mathrm{lbf}/\mathrm{in}^2 \), \(130^\text{o}\text{F} \). Calculate specific exergies for each stream.
04

- Find the rate of exergy transfer

The rate of exergy carried by each stream should be found as \( \dot{E}_\text{stream} = \dot{m} \cdot \psi \) , where \( \dot{m} \) is the mass flow rate and \(\psi\) is the specific exergy.
05

- Calculate exergy associated with heat transfer

Exergy associated with heat transfer is calculated by \( \dot{E}_{Q} = (1 - \frac{T_0}{T}) \cdot \dot{Q} \). Where \( T_0 = 70^\text{o}\text{F} \) and \(\dot{Q} \) are used along with finding \(T\) of the heat transfer process.
06

- Calculate exergy destruction

Combine the calculated information: \[ \dot{E}_{\text{destroy}} = \left( \dot{E}_{\text{in,water}} + \dot{E}_{\text{in,steam}} - \dot{E}_{\text{out,mix}} \right) - \dot{E}_\text{out,heat H} \.\]

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Key Concepts

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

exergy balance equation
The exergy balance equation is essential in thermodynamics for analyzing energy efficiency and losses. This equation tracks the exergy, or available energy, through a system. For a control volume, the exergy balance is written as: \[ \dot{E}_{\text{in}} - \dot{E}_{\text{out}} - \dot{E}_{\text{out,heat}} = \dot{E}_{\text{destroy}} \]Here, \( \dot{E}_{\text{in}} \) represents the incoming exergy, \( \dot{E}_{\text{out}} \) is the outgoing exergy, and \( \dot{E}_{\text{out,heat}} \) relates to the exergy lost as heat transfer. Finally, \( \dot{E}_{\text{destroy}} \) quantifies the exergy destroyed due to irreversibilities, such as friction and mixing.By tracking these exergy rates, the equation helps identify where energy losses occur, allowing for improvements in system efficiency.
specific exergy calculation
Specific exergy measures the useful work potential of a unit mass of the substance at a given state, relative to a reference state. We calculate it using enthalpy (\(h\)) and entropy (\(s\)) from steam tables:\[ \psi = (h - h_0) - T_0(s - s_0) \]Where:
  • \( \psi \) = Specific exergy (Btu/lb or kJ/kg)
  • \( h \), \( s \) = Specific enthalpy and entropy respectively
  • \( h_0 \), \( s_0 \) = Reference state enthalpy and entropy
  • \( T_0 \) = Reference temperature
Specific exergy captures how much energy can be converted to work. Using the steam tables, we find the necessary enthalpy and entropy values and plug them into the formula to get the specific exergy for different points in the system.
steam tables
Steam tables provide crucial thermodynamic properties of water and steam, including enthalpy (\(h\)) and entropy (\(s\)). These properties are essential for specific exergy calculations. The tables typically list values at various pressures and temperatures.Using steam tables:
  • Locate the given pressure and temperature.
  • Extract the corresponding enthalpy and entropy values.
  • Use these values in specific exergy and other thermodynamic calculations.
For example, for water at \( 20 \text{lbf}/\text{in}^2 \), \( 50^{\circ} \text{F}\), you would look up the specific enthalpy and entropy for that state. Steam tables make it easier to find these properties accurately, which is vital for any thermodynamic analysis.
mass flow rate
The mass flow rate, \( \dot{m} \), measures how much mass flows through a given point per unit time. In thermodynamics and fluid mechanics, it's vital for energy and exergy calculations. The rate of exergy carried by a stream is determined by: \[ \dot{E}_{\text{stream}} = \dot{m} \cdot \psi \]Where:
  • \( \dot{m} \) = Mass flow rate (lb/s or kg/s)
  • \( \psi \) = Specific exergy (Btu/lb or kJ/kg)
In our exercise, liquid water has a mass flow rate of \( 5 \ \text{lb}/\text{s} \) and steam has a mass flow rate of \( 0.38 \ \text{lb}/\text{s} \).By knowing the mass flow rate and specific exergy, we can compute the exergy rate for each stream and analyze the overall energy efficiency and destruction in the system.

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Most popular questions from this chapter

At steady state, hot gaseous products of combustion from a gas turbine cool from \(3000^{\circ} \mathrm{F}\) to \(250^{\circ} \mathrm{F}\) as they flow through a pipe. Owing to negligible fluid friction, the flow occurs at nearly constant pressure. Applying the ideal gas model with \(c_{p}=0.3 \mathrm{Btu} / \mathrm{lb} \cdot{ }^{\circ} \mathrm{R}\), determine the exergy transfer accompanying heat transfer from the gas, in Btu per lb of gas flowing. Let \(T_{0}=80^{\circ} \mathrm{F}\) and ignore the effects of motion and gravity.

A vessel contains \(1 \mathrm{lb}\) of air at pressure \(p\) and \(200^{\circ} \mathrm{F}\). Using the ideal gas model, plot the specific exergy of the air, in Btu/lb, for \(p\) ranging from \(0.5\) to 2 atm. The air is at rest and negligible elevation relative to an exergy reference environment for which \(T_{0}=60^{\circ} \mathrm{F}, p_{0}=1 \mathrm{~atm}\).

Air enters a turbine operating at steady state at a pressure of \(75 \mathrm{lbf} / \mathrm{in} .^{2}\), a temperature of \(800^{\circ} \mathrm{R}\), and a velocity of \(400 \mathrm{ft} / \mathrm{s}\) At the exit, the conditions are \(15 \mathrm{lbf}^{2} .^{2}, 600^{\circ} \mathrm{R}\), and \(100 \mathrm{ft} / \mathrm{s}\). There is no significant change in elevation. Heat transfer from the turbine to its surroundings at a rate of 10 Btu per lb of air flowing takes place at an average surface temperature of \(700^{\circ} \mathrm{R}\). (a) Determine, in Btu per lb of air passing through the turbine, the work developed and the exergy destruction rate. (b) Expand the boundary of the control volume to include both the turbine and a portion of its immediate surroundings so that heat transfer occurs at a temperature \(T_{0}\). Determine, in Btu per lb of air passing through the turbine, the work developed and the exergy destruction rate. (c) Explain why the exergy destruction rates in parts (a) and (b) are different. Let \(T_{0}=40^{\circ} \mathrm{F}, p_{0}=15 \mathrm{lbf} / \mathrm{in}^{2}\)

A stream of hot water at \(300^{\circ} \mathrm{F}, 500 \mathrm{lbf} / \mathrm{in}^{2}\), and a velocity of \(20 \mathrm{ft} / \mathrm{s}\) is obtained from a geothermal supply. Determine the specific flow exergy, in Btu/lb. The velocity is relative to the exergy reference environment for which \(T_{0}=77^{\circ} \mathrm{F}, p_{0}=\) \(1 \mathrm{~atm}\). Neglect the effect of gravity.

A pump operating at steady state takes in saturated liquid water at \(65 \mathrm{lbf} / \mathrm{in}^{2}\) at a rate of \(10 \mathrm{lb} / \mathrm{s}\) and discharges water at \(1000 \mathrm{lbf} / \mathrm{in}^{2}\). The isentropic pump efficiency is \(80.22 \%\). Heat transfer with the surroundings and the effects of motion and gravity can be neglected. If \(T_{0}=75^{\circ} \mathrm{F}\), determine for the pump (a) the exergy destruction rate, in Btu/s (b) the exergetic efficiency.

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