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Understanding What is the Energy Availability Equation

4 min read

According to the second law of thermodynamics, not all energy in a system is available for useful work. The concept that quantifies this useful work potential is defined by the energy availability equation, a fundamental principle known as exergy in engineering and physics.

Quick Summary

The energy availability equation, or exergy, determines the maximum useful work a system can perform as it reaches equilibrium with its surroundings. It accounts for both the quantity and quality of energy, unlike standard energy balance calculations. This analysis reveals inefficiencies and potential for optimization.

Key Points

  • Exergy is Useful Work Potential: The energy availability equation quantifies the maximum useful work a system can perform as it comes into equilibrium with its environment.

  • Availability Depends on the System: The specific form of the energy availability equation differs for closed systems (non-flow) and open systems (steady-flow).

  • Irreversibility Destroys Exergy: Unlike energy, which is conserved, exergy is always destroyed in any real, irreversible process, such as friction or heat transfer.

  • Environmental Reference is Key: The calculation of exergy is dependent on defining a 'dead state' or reference environment, which is the baseline for maximum work potential.

  • Gibbs Free Energy is Specific Exergy: The Gibbs free energy equation is a special case of the availability equation used to determine maximum non-expansion work at constant temperature and pressure.

  • Exergy Reveals True Inefficiencies: Exergy analysis provides a more realistic measure of efficiency than first law energy analysis because it accounts for the destruction of work potential.

In This Article

What is the energy availability equation?

The energy availability equation, also known as exergy, quantifies the maximum amount of useful work that can be extracted from a system as it undergoes a reversible process to reach equilibrium with its environment, a state referred to as the 'dead state'. Unlike energy, which is conserved, exergy can be destroyed by irreversibilities such as friction or heat transfer across a finite temperature difference. The specific form of the availability equation depends on the type of system being analyzed—whether it is a closed system (non-flow) or an open system (steady-flow).

The energy availability equation for a closed system

For a closed system, which exchanges energy but not mass with its surroundings, the change in availability ($\Delta A$) between an initial state 1 and a final state 2 is defined by the following equation:

$\Delta A = (U_1 - U_2) - T_0(S_1 - S_2) + P_0(V_1 - V_2)$

  • $U_1$ and $U_2$ are the internal energies of the system at the initial and final states.
  • $T_0$ is the absolute temperature of the environment (the dead state).
  • $S_1$ and $S_2$ are the entropies of the system at the initial and final states.
  • $P_0$ is the absolute pressure of the environment.
  • $V_1$ and $V_2$ are the volumes of the system at the initial and final states.

This equation reveals that the useful work potential is influenced by changes in internal energy, the heat exchanged with the environment due to entropy changes, and the boundary work done by the system against the environment's pressure. The term $-T_0(S_1 - S_2)$ represents the energy that becomes unavailable for work due to entropy changes, which is a direct consequence of the second law of thermodynamics.

The Gibbs free energy as a special case

The Gibbs free energy equation, $\Delta G = \Delta H - T\Delta S$, is a specific instance of the availability equation, relevant for processes occurring at a constant temperature and pressure. It represents the maximum non-expansion work that can be extracted from a system under these specific conditions. The Gibbs free energy is therefore a measure of chemical availability, determining the spontaneity of chemical reactions.

The energy availability equation for a steady-flow system

In an open system, or steady-flow process, both mass and energy can cross the control volume boundaries. The maximum useful work (or shaft work, $W_{sh, max}$) is described by the following equation, which accounts for changes in enthalpy, entropy, kinetic energy, and potential energy between the inlet and outlet:

$W_{sh, max} = (H_1 - H_0) - T_0(S_1 - S_0) + \frac{C_1^2 - C_0^2}{2} + g(Z_1 - Z_0)$

This is often simplified by the steady-flow availability function, $B = H - T_0S$, where the maximum useful work is the change in B ($B_1 - B_0$) between the initial and dead states. The additional terms for kinetic ($C^2/2$) and potential ($gZ$) energy are also considered when significant.

Factors influencing energy availability

Several factors affect a system's total energy availability, often leading to a reduction in potential useful work:

  • Irreversibilities: All real-world processes are irreversible, meaning they involve friction, heat transfer over finite temperature differences, and mixing. These processes generate entropy, which in turn destroys exergy.
  • Temperature difference: The maximum efficiency of a heat engine is determined by the Carnot efficiency, which depends on the temperature difference between the heat source and sink. A larger temperature gradient translates to higher thermal exergy.
  • Chemical potential: For systems involving chemical reactions, the difference in chemical potential between substances and their reference state environment determines the chemical exergy. This is a crucial factor in fuel cell and combustion analysis.
  • System properties: The internal energy, entropy, pressure, and volume of a system all affect its availability. Exergy is a property that depends on both the system's state and the defined reference environment.
  • Kinetic and potential energy: While often negligible in thermodynamic analysis, significant changes in a system's velocity or elevation relative to the dead state can contribute to its total availability. For instance, the exergy of wind is its kinetic energy relative to the calm atmosphere.

Comparison of Energy (First Law) vs. Exergy (Second Law) Analysis

Feature First Law (Energy) Analysis Second Law (Exergy) Analysis
Core Concept Conservation of energy: Energy can be neither created nor destroyed. Destruction of available work: Exergy is always destroyed in real processes.
Efficiency Measure Thermal efficiency ($\eta$): Measures energy output relative to energy input. Can exceed 100% for heat pumps. Exergy efficiency ($\epsilon$): Measures exergy output relative to exergy input. Always less than or equal to 100%.
Energy Quality Does not differentiate between energy quality. All forms of energy are treated as equivalent. Distinguishes between energy quality. High-grade energy (electricity) has higher exergy than low-grade energy (heat).
Reference State Not required for calculations. Depends on a reference state (the dead state) for the environment.
Identifies Losses Identifies energy losses from the system, like heat transfer to surroundings. Identifies both exergy losses (to surroundings) and exergy destruction (internal irreversibilities).
Primary Insight Total energy balance for a system. The potential for process improvement by minimizing irreversibilities.

Conclusion

The energy availability equation, or exergy, is a powerful tool derived from the second law of thermodynamics that allows for a deeper understanding of energy systems beyond the simple first law energy balance. By quantifying the maximum useful work potential relative to a reference environment, exergy analysis highlights inefficiencies and the true 'quality' of energy. Whether for a closed system using the availability function $\phi = U + P_0V - T_0S$ or a steady-flow system using the function $B = H - T_0S$, the calculation of exergy provides a critical metric for optimizing energy conversion and usage. Understanding and minimizing the destruction of exergy is key to improving the efficiency and sustainability of any energy-dependent process.

For further reading, the thermodynamic concepts of exergy and availability are comprehensively covered in the Wikipedia article on Exergy.

Frequently Asked Questions

Energy, per the first law of thermodynamics, is conserved and cannot be created or destroyed. Energy availability, or exergy, is the portion of energy that can be converted into useful work and is destroyed by inefficiencies, as dictated by the second law of thermodynamics.

The 'dead state' is the state of a system when it is in thermodynamic equilibrium with its environment. At this point, the system has reached the lowest possible energy state and no further useful work can be extracted from it.

The availability for a closed system can be calculated using the equation $\Delta A = (U_1 - U_2) - T_0(S_1 - S_2) + P_0(V_1 - V_2)$, where U is internal energy, S is entropy, T0 and P0 are environmental temperature and pressure, and V is volume.

Entropy represents the energy that is unavailable for useful work. As irreversible processes increase a system's entropy, more energy becomes 'unavailable' to do work, thus decreasing the system's exergy.

Exergy analysis provides a more powerful tool for system optimization because it identifies not only where energy is lost but also where it is destroyed due to inefficiencies. This allows engineers to pinpoint the true potential for performance improvement.

Exergy is destroyed by irreversibilities inherent in real processes. Common causes include friction, unrestrained expansion, heat transfer across finite temperature differences, mixing of different substances, and chemical reactions.

Gibbs free energy ($Δ$G) is a specific type of exergy calculation. It represents the maximum non-expansion useful work for a system operating at constant temperature and pressure, which is a condition frequently met in chemical applications.

References

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Medical Disclaimer

This content is for informational purposes only and should not replace professional medical advice.