I'll go over all of these equations.
Extensive/intensive (Schroeder 5.2)
If you consider two identical systems taken together (e.g. two cups of water, or two identical cubes of metal), each thermodynamic property either doubles or remains the same.
 Extensive
 An extensive property, such as mass will double when you’ve got twice as much stuff.
 Intensive
 An intensive property, such as density will be the same regardless of how much stuff you’ve got.
We care about extensivity and intensivity for several reasons. In one sense it functions like dimensions as a way to check our work. In another sense, it is a fundamental aspect of each measurable property, and once you are accustomed to this, you will feel very uncomfortable if you don’t know whether it is extensive or intensive.
How to measure things
I may give you questions which require you to make use of these definitions.
 Volume
 Measure dimensions and compute it. (extensive)
 Pressure
 Force per area. Can equalize if systems can exchange volume. (intensive) (Schroeder 1.2)
 Temperature
 Find something that depends on temperature, and calibrate it. Alternatively use an ideal gas. Equalizes when systems are in contact. (intensive)
 Energy
 Challenging... measure work and heat (e.g. by measuring power into resistor) and use the First Law. (extensive)
\begin{align}
W = \int pdV
\end{align}
 Entropy
 (extensive) Measure heat for a quasistatic process and find
\begin{align}
\Delta S &= \int \frac{{\mathit{\unicode{273}}} Q}{T}
\end{align}
(Schroeder 3.2)
 Derivatives
 Measure changes of one thing as the other changes, with the right stuff held fixed.
First Law (Energy conservation, Schroeder 1.4)
\begin{align}
dU &= {\mathit{\unicode{273}}} Q + {\mathit{\unicode{273}}} W
\end{align}
Second Law (Entropy increases, Schroeder 2.3)
\begin{align}
\Delta S_{\text{system}} + \Delta S_{\text{environment}} \ge 0
\end{align}
Thermodynamic identity (Schroeder 3.4)
\begin{align}
dU &= TdS  pdV
\end{align}
Total differentials
When we have a total differential, the things in front of the \(dS\),
\(dV\), etc are partial derivatives.
\begin{align}
T &= \left(\frac{\partial U}{\partial S}\right)_V &
p &= \left(\frac{\partial U}{\partial V}\right)_S
\end{align}
Also, you can integrate along a path using a total differential, and
can do linear algebra using total differential equations,
e.g. substituting one for another. Fun example:
\begin{align}
dS &= \frac{1}{T}dU + \frac{p}{T}dV \\
\frac1{T} &= \left(\frac{\partial S}{\partial U}\right)_V &
\frac{p}{T} &= \left(\frac{\partial S}{\partial V}\right)_U
\end{align}
(the second derivative shown here is known as the cyclic chain rule in a
more general sense)
Thermodynamic potentials (Schroeder 1.6, 5.1)
 Helmholtz free energy

\begin{align}
F &= U  TS \\
dF &= dU  TdS  SdT \\
&= SdT pdV
\end{align}
 Enthalpy

\begin{align}
H &= U + pV \\
dH &= dU + pdV + Vdp \\
&= TdS + Vdp
\end{align}
 Gibbs free energy

\begin{align}
G &= H  TS \\
&= U TS+pV \\
dG &= dH  TdS  SdT \\
&= SdT +Vdp
\end{align}
Maxwell relations
You should be able to use the fact that mixed partial derivatives do not depend on the order taken to find Maxwell relations. Also using the differentials above, e.g.
\begin{align}
\left(\frac{\partial {\left(\frac{\partial {G}}{\partial {T}}\right)_{p}}}{\partial {p}}\right)_{T}
&=\left(\frac{\partial {\left(\frac{\partial {G}}{\partial {p}}\right)_{T}}}{\partial {T}}\right)_{p}
\\
\left(\frac{\partial {S}}{\partial {p}}\right)_{T} &= \left(\frac{\partial {V}}{\partial {T}}\right)_{p}
\end{align}
Statistical entropy (Schroeder 2.6, Problem 6.43)
Boltzmann formulation (microcanonical or for large \(N\)):
\begin{align}
S(E) &= k_B \ln g(E)
\end{align}
where \(g\) is the number of microstates (or energy eigenstates).
We spent little time on the Boltzmann formulation, but it is helpful to
know that at sufficiently high temperatures the entropy approaches
\(k_B\) times the logarithm of the number of energy eigenstates.
Gibbs formulation (always true):
\begin{align}
S(E) &= k_B \sum_{i}^{\text{all states}} P_i \ln P_i
\end{align}
Boltzmann ratio (Schroeder 6.1)
\begin{align}
\frac{P_i}{P_j} &= e^{\frac{E_i  E_j}{k_BT}} \\
P_i &= \frac{e^{\frac{E_i}{k_BT}}}{Z}
\\
Z &= \sum_j^{\text{all states}} e^{\frac{E_j}{k_BT}}
\end{align}
Thermal averages (Schroeder 6.2)
The average value of any quantity is given by the weighted average
\begin{align}
\left<X\right> &= \sum_i^{\text{all states}} P_i X_i
\end{align}
In particular, the internal energy is given by
\begin{align}
U &= \sum_i^{\text{all states}} P_i E_i
\end{align}
Helmholtz free energy from statistics
\begin{align}
F &= kT\ln Z
\end{align}
The following is the old review that I wrote.
Math
Total Differentials
\begin{align}
dA &= \left(\frac{\partial {A}}{\partial {B}}\right)_{C}dB + \left(\frac{\partial {A}}{\partial {C}}\right)_{B}dC
\end{align}
You can:
 Do algebra
 Interpret coefficients as partial derivatives
 Integrate
Mixed partial derivatives
\begin{align}
\left(\frac{\partial {\left(\frac{\partial {A}}{\partial {B}}\right)_{C}}}{\partial {C}}\right)_{B} =
\left(\frac{\partial {\left(\frac{\partial {A}}{\partial {C}}\right)_{B}}}{\partial {B}}\right)_{C}
\end{align}
Chain rules (need not be memorized, but may be used)
\begin{align}
\left(\frac{\partial {A}}{\partial {B}}\right)_{C} &= \frac{1}{\left(\frac{\partial {B}}{\partial {A}}\right)_{C}}
\\
\left(\frac{\partial {A}}{\partial {B}}\right)_{D} &= \left(\frac{\partial {A}}{\partial {C}}\right)_{D}\left(\frac{\partial {C}}{\partial {B}}\right)_{D}
\\
\left(\frac{\partial {A}}{\partial {B}}\right)_{C} &= \frac{\left(\frac{\partial {A}}{\partial {C}}\right)_{B}}{\left(\frac{\partial {B}}{\partial {C}}\right)_{A}}
\end{align}
Thermodynamics
Entropy
\begin{align}
\Delta S &= \int {\mathit{\unicode{273}}} \frac{Q_{\text{quasistatic}}}{T}
\\
{\mathit{\unicode{273}}} Q &= TdS
\\
C_\alpha &= T \left(\frac{\partial {S}}{\partial {T}}\right)_{\alpha}
\end{align}
First Law
\begin{align}
\Delta U &= Q + W
\\
dU &= {\mathit{\unicode{273}}} Q + {\mathit{\unicode{273}}} W
\\
dU &= TdS  pdV
\end{align}
Second Law
\begin{align}
\Delta S_{\text{system}} + \Delta S_{\text{surroundings}} \ge 0
\end{align}
Legendre Transforms
You can subtract \(TS\) from \(U\) or add \(pV\) to \(U\) to create new thermodynamic potentials that are convenient when \(T\) or \(p\) are held fixed or controlled.
Maxwell Relations
From any thermodynamic potential you can use the equality of mixed partial derivatives to create a relationship between two different partial derivatives.
Statistical Mechanics
\begin{align}
P_i &= \frac{e^{\beta E_i}}{Z}
\\
Z &= \sum_i^{\text{all states}} \frac{e^{\beta E_i}}{Z}
\\
\beta &= \frac{1}{k_BT}
\\
F &= k_BT \ln Z
\\
U &= \sum_i^{\text{all states}} P_i E_i
\\
S &= k_B\sum_i^{\text{all states}} P_i \ln P_i
\end{align}