Say we are undergoing an isothermal process that eventually settles at equilibrium. $F$ will minimize at equilibrium, and if the entropy of the system is not held constant $U$ will not. Why do we care though? What do we afford to lose if we use $U$ anyway? What use do we have for $F$ if it has this property for isothermal processes?

Gibbs free energy minimizes only at constant pressure and temperature, so to me it sounds like a less general version of Helmholtz free energy. So why is it used?

Foundations

In a closed system, the four combined laws of thermodynamics are as follows:

$$ dU = TdS - pdV $$
$$ dH = TdS + Vdp $$
$$ dA = -SdT - pdV $$
$$ dG = -SdT + Vdp $$

You can obtain these in one of two ways. You can start from the first law (the first equation above) and apply the definitions of enthalpy, Helmholz energy, and Gibbs energy. Alternatively, you can start from the postulates of $U(V,n)$ and $S(U,n)$ and work through Legendre transforms. The imperative appreciation here is that derivations of these equations is NOT based on statements about what kind of process is occurring. They are fundamental and absolute expressions.

The other imperative statement is that we always need two and only two parameters to define the exact mechanical, thermal, chemical, and therefore thermodynamic state of a closed system with a pure substance. It is a statement of the Gibbs phase rule $F_max = (C - R) - Pi_min + 2 = (1 - 0) - 1 + 2 = 2$. This establishes why the expansions below consider only two parameters and no more as requirements to set the thermodynamic criteria for equilibrium or spontaneity.

Equilibrium

At equilibrium, a system must show no change in any state property. By review of the combined laws

• A process that occurs at constant entropy and volume will show no change in $U$
  


• A process that occurs at constant entropy and pressure will show no change in $H$
  


• A process that occurs at constant temperature and volume will show no change in $A$
  


• A process that occurs at constant temperature and pressure will show no change in $G$
  

This establishes the four criteria for equilibrium of any process.

• 
  $Delta U = 0$ at constant $(S, V)$
  


• 
  $Delta H = 0$ at constant $(S, p)$
  


• 
  $Delta A = 0$ at constant $(T, V)$
  


• 
  $Delta G = 0$ at constant $(T, p)$
  

We live (mostly) in a constant temperature + pressure world. Therefore, to determine whether a system is or is not at equilibrium, we work with (engineer processes using) changes in the Gibbs energy more than any of the other thermodynamic state functions.

Spontaneity

A process that is occurring in one of the four realms and is not at equilibrium must have a change in the respective state function that itself is not zero. We apply a systematic analysis starting from the Clausius form of the second law (heat flows spontaneously from hot to cold) to establish the convention for $dU$ in spontaneous processes. The rest of the expressions follow from it.

• 
  $Delta U < 0$ at constant $(S, V)$
  


• 
  $Delta S > 0$ at constant $(U, V)$
  


• 
  $Delta H < 0$ at constant $(S, p)$
  


• 
  $Delta A < 0$ at constant $(T, V)$
  


• 
  $Delta G < 0$ at constant $(T, p)$
  

Utility

One or the other of the expressions above is never more (or less) "useful". The framework is always first to define what parameters are held constant as the process occurs. That step defines which state function is to be used to establish equilibrium or spontaneity.

The mechanical work of a reversible process is always $w = pm int p dV$ (I leave the sign convention here as a hot discussion point that IUPAC folks and engineers banter over). Other work may be obtained from a process when it is spontaneous in constant $T, V$ or constant $T, p$ space. This is how we relate changes in Helmholtz or Gibbs energy to "free" work of a process.

$U$ (or actually $S$) is only relevant for an isolated system. This is not the case, for example, when you keep the temperature constant, since then heat must flow from the environment to your system (or vice versa) for $T$ to remain fixed.

But let's say the system you are interested in is small compared to the environment. Keeping track after all the thermodynamics of the surroundings is difficult, so we want to somehow treat the system alone without having to think all the time on what is happening outside. The way to do it, in the case of thermal contact only, is to define the Helmholtz free energy

$$F=U-TS$$

Here $U$ is the energy of the system, $S$ is its entropy but $T$ is the temperature of the environment (and it is fixed since your system is so small so that practically it has no effect on it). When $F$ is minimized, it can be shown (see here) that the entropy of the system + the environment is maximized, which is the condition you would expect for a system in thermal equilibrium.

Similarly, if your system can only exchange volume with the environment, the quantity that is minimized is known at the enthalpy

$$H=U+PV$$

In the case of both heat and volume exchange, you would use the Gibbs free energy

$$G=U-TS+PV$$

There is also a mathematical-inclined argument for this. You know that

$$rm dF=-Srm dT-Prm dV$$

so the natural variables of $F$ are $T$ and $V$, i.e. $F=Fleft(T,Vright)$. It means that $F$ is the right function to use if you can control both $T$ and $V$, which is the case for a system of constant volume in contact with a thermal bath. In the other cases

$$rm dH=Trm dS+Vrm dPLongrightarrow H=Hleft(S,Pright)$$

and

$$rm dG=-Srm dT+Vrm dPLongrightarrow G=Gleft(T,Pright)$$

You can clearly see which variables you can control and consequently which situations each thermodynamic potential fits. This mathematical trick of changing the variables of your function is known as the Legendre transformation. This is exactly the same as the relation between Lagrangians and Hamiltonians in classical mechanics.

To finish with an example, when treating liquid-gas phase transitions, it is customary to use the Gibbs free energy. This is the right thermodynamic potential since your system can exchange both its entropy $S$ and volume $V$ with the outside, such that the variables you control (the environment) are the corresponding conjugate variables - the temperature $T$ and the pressure $P$ respectively.