ESCI 341 – Atmospheric Thermodynamics

Lesson 10 – The Energy Minimum Principle

 

References:    Thermodynamics and an Introduction to Thermostatistics, Callen

Physical Chemistry, Levine

 

THE ENTROPY MAXIMUM PRINCIPLE

l  We’ve seen that a reversible process achieves maximum thermodynamic efficiency.

l  Imagine that I am adding heat to a system (dQin), converting some of it to work (dW), and discarding the remaining heat (dQout).

l  We’ve already demonstrated that dQout cannot be zero (this would violate the second law).

l  We also have shown that dQout will be a minimum for a reversible process.  This means that the differential of heat for the system (dQ = dQin - dQout) will be a maximum for the reversible process,

.

l  The change in entropy of the system, dS, is defined as dQrev/T.  We can thus write the inequality

,

or

l  For an isolated system (dQ = 0) the inequality becomes

,

which is just a restatement of the second law of thermodynamics.

l  We can divide this expression by dt and find that

.

l  For an unconstrained, isolated system irreversible process will operate and increase the total entropy of the system until equilibrium is reached.  Once equilibrium is reached,

,

and the irreversible processes will cease.

l  This is the entropy maximum principle.  It states that

o        For an isolated, unconstrained system, the equilibrium state will be that state which has the maximum entropy for a given internal energy.

l  An example of application of the entropy maximum principle is an isolated metal bar that is initially hotter at one end than another.  The temperature distribution that maximizes the entropy is one that is uniform (isothermal).  Therefore, if left alone, the temperature will spontaneously adjust to an isothermal distribution.

l  Some authors have mistakenly applied the entropy maximum principle in an attempt to explain why a well-mixed layer of air has an adiabatic temperature profile.  However, it turn out that an isothermal layer has greater entropy than any other temperature profile for the same static energy.  This was shown by J. Willard Gibbs in 1928 (Collected Works of J. Willard Gibbs, Vol I: Thermodynamics, pp. 145).

 

THE ENERGY MINIMUM PRINCIPLE

l  The first law for can be written as

,

so that we arrive at another useful inequality,

,

or

.

l  This inequality tells us that, for a system at constant entropy and volume,

.

o        This means that the system held at constant entropy and volume will continue to change until it reaches a point where dU/dt = 0.  At this point, the internal energy, U, will be a minimum and the system will be in material equilibrium.

l  This principle is known as the energy minimum principle.  It states that

o        For an unconstrained system at constant volume and entropy, the equilibrium state will be that state which has the minimum internal energy.

l  The energy minimum principle was derived from the entropy maximization principle.  The energy minimum principle and the entropy maximum principle are complimentary.

 

ENTHALPY

l  Beginning with

and writing

we get

.

l  We’ve seen the combination U + pV before…it is another state function called enthalpy (H).  Therefore,

.

l  For processes occurring at constant entropy and pressure,

.

l  An unconstrained system at constant entropy and pressure will spontaneously evolve into a state that minimizes enthalpy.

l   This principle is known as the enthalpy minimum principle.  It states that

o        For an unconstrained system at constant pressure and entropy, the equilibrium state will be that state which has the minimum enthalpy.

 

 

HELMHOLTZ FREE ENERGY

l  The energy and enthalpy minimum principles aren’t often very handy for solving problems, since we don’t really work with many processes that occur at constant entropy.  It would be nice, therefore, to have some way of expressing a minimum principle in terms of processes where entropy is allowed to change.

l  We do this by starting with

.

o        From the product rule for differentiation we have

.

o        This means we can write the inequality as

.

l  The quantity (U - TS) is another state variable, and we name it the Helmholtz free energy (F º U - TS). 

l  For processes that occur under constant temperature and volume,

.

l  This principle is known as the Helmholtz free energy minimum principle.  It states that

o        For an unconstrained system at constant temperature and volume, the equilibrium state will be that state which has the minimum Helmholtz free energy.

l  Notice that for a reversible process, if temperature is held constant, then dF -pdV.  We can therefore interpret F as the work that can be extracted from a constant temperature process.

 

GIBBS FREE ENERGY

l  The Helmholtz free energy is handy for processes that occur at constant temperature and volume.  In the atmosphere, however, we frequently are dealing with processes that occur at constant temperature and pressure.  It would be nice to have another form of the energy minimum principle that we can apply to these processes.

l  If we start with the enthalpy form

and substitute

we get

.

l  The quantity (H - TS) is another state variable, and we name it the Gibbs free energy (G º H - TS). 

l  For processes that occur under constant temperature and pressure,

.

l  This principle is known as the Gibbs free energy minimum principle.  It states that

o        For an unconstrained system at constant temperature and pressure, the equilibrium state will be that state which has the minimum Gibbs free energy.

l  U, H, F, and G are referred to as thermodynamic potentials.  The expressions for each are summarized below

 

MAXWELL RELATIONS

l  Under equilibrium conditions, the thermodynamic potentials are minimized.  We therefore can write the following equations, known as the Gibbs equations, for equilibrium states

                     Gibbs equations

l  The Gibbs equations are exact differentials (because they are differentials of state functions).  One property of exact differentials is that if df(x,y) = Mdx +Ndy, then

.                   Euler reciprocity relation

This is because

so that

and partial derivatives commute, so that

.

l  This allows us to write, from the Gibbs equations,