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Determine the specific flow exergy, in Btu/lbmol and Btu/ lb, at \(440^{\circ} \mathrm{F}, 73.5 \mathrm{lbf} / \mathrm{in}^{2}\). for (a) nitrogen \(\left(\mathrm{N}_{2}\right)\) and (b) carbon dioxide \(\left(\mathrm{CO}_{2}\right)\), each modeled as an ideal gas, and relative to an exergy reference environment for which \(T_{0}=77^{\circ} \mathrm{F}, p_{0}=\) \(14.7 \mathrm{lbf} / \mathrm{in}^{2}\) Ignore the effects of motion and gravity.

Short Answer

Expert verified
Calculate specific exergy using formulas for h and s, convert units to Btu/lb and Btu/lbmol for both Nâ‚‚ and COâ‚‚.

Step by step solution

01

Define given data and convert units

Given: Temperature: 440°F, which is equivalent to 500.37 K using the formula \[ T(K) = \left( T(°F) + 459.67 \right) \times \frac{5}{9} \] Pressure: 73.5 lbf/in², which is equivalent to 506.62 kPaReference environment: \( T_0 = 77°F = 298.15 K \)\( p_0 = 14.7 lbf/in² = 101.3 kPa \)
02

Determine properties of nitrogen (N2) and carbon dioxide (CO2)

Molar mass of \( \mathrm{N_2} \) = 28.0134 g/mol Molar mass of \( \mathrm{CO_2} \) = 44.01 g/mol For simplicity, we will assume the gas constant \( R \) remains constant for ideal gases: R = 8.314 J/(mol·K) or 0.08206 L·atm/(mol·K)
03

Calculate specific flow exergy for nitrogen \( \mathrm{N_2} \)

Using the formula for specific exergy: \[ e = (h - h_0) - T_0 (s - s_0) \]Where:\( h - h_0 = C_p (T - T_0) \)and \[ s - s_0 = C_p \ln \left( \frac{T}{T_0} \right) - R \ln \left( \frac{p}{p_0} \right) \]Assuming ideal gas properties:\( C_p (\mathrm{N_2}) = 29.1 \text{ J/(mol·K)} \)Substitute values to find \( e \):\( h - h_0 = 29.1 \times (500.37 - 298.15) \)\( s - s_0 = 29.1 \times \ln \left( \frac{500.37}{298.15} \right) - 8.314 \times \ln \left( \frac{506.62}{101.3} \right) \)Calculate exergy: \( e = (h - h_0) - 298.15 \times (s - s_0) \)
04

Calculate specific flow exergy for carbon dioxide \( \mathrm{CO_2} \)

Using the same formula for specific exergy: \[ e = (h - h_0) - T_0 (s - s_0) \]Where:\( h - h_0 = C_p (T - T_0) \)and \[ s - s_0 = C_p \ln \left( \frac{T}{T_0} \right) - R \ln \left( \frac{p}{p_0} \right) \]Assuming ideal gas properties:\( C_p \left( \mathrm{CO_2} \right) = 37.0 \text{ J/(mol·K)} \)Substitute values to find \( e \):\( h - h_0 = 37.0 \times (500.37 - 298.15) \)\( s - s_0 = 37.0 \times \ln \left( \frac{500.37}{298.15} \right) - 8.314 \times \ln \left( \frac{506.62}{101.3} \right) \)Calculate exergy: \( e = (h - h_0) - 298.15 \times (s - s_0) \)
05

Convert exergy to Btu/lb and Btu/lbmol

Convert the specific exergy obtained from J/mol to Btu/lb and Btu/lbmol using the conversion factors: 1 J = 0.000947817 BtuMolar mass of \( \mathrm{N_2} = 28.0134 \text{ g/mol} \)Molar mass of \( \mathrm{CO_2} = 44.01 \text{ g/mol} \)For Nitrogen:\[ e_{N_2} (\text{Btu/lb}) = e_{N_2} (\text{J/mol}) \times 0.000947817 \times \frac{1}{28.0134} \]For Carbon Dioxide:\[ e_{CO_2} (\text{Btu/lb}) = e_{CO_2} (\text{J/mol}) \times 0.000947817 \times \frac{1}{44.01} \]Finally, calculate the exergy values.

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Key Concepts

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

thermodynamics
Thermodynamics is the branch of physics that deals with heat, work, and energy, and the laws governing their interactions. It is fundamental in understanding how energy systems work and is divided into four main laws: the Zeroth, First, Second, and Third Laws of Thermodynamics.

In simple terms, these laws explain how energy is conserved, how it flows, and how it affects matter. For example, the First Law of Thermodynamics, also known as the Law of Energy Conservation, states that energy cannot be created or destroyed; it can only be transferred or converted from one form to another.

Understanding thermodynamics is crucial for solving problems related to energy transfer in any form, including calculating the specific flow exergy we are tackling in this exercise.
ideal gas law
The Ideal Gas Law is a fundamental equation in thermodynamics that relates pressure, volume, temperature, and the number of moles of an ideal gas. The equation is \[ PV = nRT \]Here,
  • P = Pressure
  • V = Volume
  • n = Number of moles
  • R = Universal gas constant
  • T = Temperature in Kelvin
The Ideal Gas Law assumes that gas molecules do not interact and occupy no volume, which is a good approximation under many conditions.

For our specific exergy calculation problem, we model nitrogen (\(N_2\)) and carbon dioxide (\(CO_2\)) as ideal gases. This lets us use simplified properties and constants, making the math more manageable.

Remember, the better we stick to the Ideal Gas Law assumptions, the more accurate our calculations will be.
specific exergy
Specific exergy refers to the maximum useful work obtainable from a system as it reaches equilibrium with a reference environment. It combines both physical and chemical properties and is calculated using the formula:\[ e = (h - h_0) - T_0 (s - s_0) \]where
  • \(h\) = Specific enthalpy
  • \(h_0\) = Specific enthalpy of the reference environment
  • \(T_0\) = Temperature of the reference environment
  • \(s\) = Specific entropy
  • \(s_0\) = Specific entropy of the reference environment
Specific exergy is vital in thermodynamics because it quantifies the potential work available from thermal processes.

In our problem, we calculate the specific exergy for \(N_2\) and \(CO_2\) at given conditions. This helps us understand how effectively these gases can be used for work compared to their state in a reference environment.
enthalpy
Enthalpy is a measure of the total energy of a thermodynamic system, including internal energy plus the product of pressure and volume: \[ H = U + PV \]where
  • \(H\) = Enthalpy
  • \(U\) = Internal energy
  • \(P\) = Pressure
  • \(V\) = Volume
In our calculations, we use specific enthalpy (\(h\)), expressed per unit of mass or mole. For an ideal gas, the change in specific enthalpy with temperature can be found using \(h - h_0 = C_p (T - T_0)\), where \(C_p\) is the specific heat capacity at constant pressure.

Enthalpy is important because it helps us determine the energy changes in the system due to heat transfer and work done at constant pressure.

Understanding enthalpy changes is key to calculating the specific exergy for nitrogen and carbon dioxide in this problem.
entropy
Entropy is a measure of a system's disorder or randomness, and it indicates the amount of energy unavailable for doing useful work. The Second Law of Thermodynamics states that entropy always increases in an isolated system.\[ S_{total} = S_{system} + S_{surroundings} \]where
  • \(S\) = Entropy
In thermodynamic calculations, changes in specific entropy (\(s\)) are critical. For an ideal gas, the change in specific entropy due to temperature and pressure can be calculated as:\[ s - s_0 = C_p \ln \left( \frac{T}{T_0} \right) - R \ln \left( \frac{p}{p_0} \right) \]where \(C_p\) is the specific heat capacity at constant pressure, \(T\) and \(p\) are the temperature and pressure, and \(R\) is the gas constant.

The entropy change helps us find the proportion of energy that cannot be used for useful work, making it indispensable for determining specific exergy.

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Most popular questions from this chapter

When matter flows across the boundary of a control volume, an energy transfer by work, called flow work, occurs. The rate is \(\dot{m}(p v)\) where \(\dot{m}, p\), and \(v\) denote the mass flow rate, pressure, and specific volume, respectively, of the matter crossing the boundary (see Sec. 4.4.2). Show that the exergy transfer accompanying flow work is given by \(\dot{m}\left(p v-p_{0} v\right)\), where \(p_{0}\) is the pressure at the dead state.

Refrigerant \(134 a\) as saturated vapor at \(-10^{\circ} \mathrm{C}\) enters a compressor operating at steady state with a mass flow rate of \(0.3 \mathrm{~kg} / \mathrm{s}\). At the compressor exit the pressure of the refrigerant is 5 bar. Stray heat transfer and the effects of motion and gravity can be ignored. If the rate of exergy destruction within the compressor must be kept less than \(2.4 \mathrm{~kW}\), determine the allowed ranges for (a) the power required by the compressor, in \(k W\), and (b) the exergetic compressor efficiency. Let \(T_{0}=298 \mathrm{~K}, p_{0}=1\) bar.

A domestic water heater holds \(189 \mathrm{~L}\) of water at \(60^{\circ} \mathrm{C}\), \(1 \mathrm{~atm}\). Determine the exergy of the hot water, in \(\mathrm{kJ}\). To what elevation, in \(m\), would a \(1000-\mathrm{kg}\) mass have to be raised from zero elevation relative to the reference environment for its exergy to equal that of the hot water? Let \(T_{0}=298 \mathrm{~K}\), \(p_{0}=1 \mathrm{~atm}, \mathrm{~g}=9.81 \mathrm{~m} / \mathrm{s}^{2}\).

Water vapor enters a valve with a mass flow rate of \(2 \mathrm{~kg} / \mathrm{s}\) at a temperature of \(320^{\circ} \mathrm{C}\) and a pressure of 60 bar and undergoes a throttling process to 40 bar. (a) Determine the flow exergy rates at the valve inlet and exit and the rate of exergy destruction, each in \(\mathrm{kW}\). (b) Evaluating exergy at \(8.5\) cents per \(\mathrm{kW} \cdot \mathrm{h}\), determine the annual cost, in \(\$ /\) year, associated with the exergy destruction, assuming 8400 hours of operation annually. Let \(T_{0}=25^{\circ} \mathrm{C}, p_{0}=1\) bar.

An ideal gas is stored in a closed vessel at pressure \(p\) and temperature \(T\). (a) If \(T=T_{0}\), derive an expression for the specific exergy in terms of \(p, p_{0}, T_{0}\), and the gas constant \(R\). (b) If \(p=p_{0}\), derive an expression for the specific exergy in terms of \(T, T_{0}\), and the specific heat \(c_{p}\), which can be taken as constant. Ignore the effects of motion and gravity.

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