Use the definition of pressure. Because the force increases, the pressure must also increase, since the area of the piston remains the same.
Use the relationship between entropy and energy transferred by heating. Because the piston is insulated, there is no heating, and since the process is presumed to be reasonably slow when I add a few masses, the entropy should not change.
Use the First Law. The masses do work on the system, and since there is no heating, the internal energy must increase. We know that the masses will do work because the gas will compress, which means the potential energy of the masses will decrease (i.e. they lose energy). Or alternatively you could determine this algebraically by using \({\mathit{\unicode{273}}} W = -pdV\) and since \(dV<0\) the work must be positive, meaning the system gains energy by working.
Check dimensions and whether extensive is added to extensive. In this case extensivity works out because the only extensive variables are \(U\), \(S\) and \(N\), which makes each of the three terms also extensive (\(U\), \(pS\), and \( \frac32 Nk_BT\)).
When we check dimensions, each term must be an energy, since \(U\) is an energy. Pressure is a force per area, and entropy is an energy per temperature (as you can tell since \({\mathit{\unicode{273}}} Q=TdS\)). These multiplied will not give us an energy, so the equation must be wrong.
Check dimensions and whether extensive is equal to extensive. Both sides are extensive, and both sides are energies. You can remember that \(pV\) is an energy because \({\mathit{\unicode{273}}} W = -pdV\).
Check dimensions and whether extensive is added to extensive.
This one is a bit trickier. Both sides are energies, because \(k_BT\) is an energy and \(N\) is dimensionless. So our dimensions work out fine.
The tricky bit here is to examine extensivity. \(U=Nk_BT\) works fine for extensivity, since \(U\) and \(N\) are both extensive. What causes us trouble (and makes this wrong) is \(1+N\), since the number 1 is not extensive and thus shouldn't be added to \(N\).
Consider the variable \(F\) defined by \begin{align} F = U - TS \end{align} where \(U\) is the internal energy, \(T\) is the temperature, and \(S\) is the entropy. Solve for the partial derivative \(\left(\frac{\partial F}{\partial T}\right)_V\) where \(V\) is the volume.
Hint: The partial derivative is defined by the ratio of small changes in \(F\) and \(T\) that would take us to a new state without changing volume. Since the changes are small, we can assume the change happens via a quasi-static process. Therefore, we know that the thermodynamic identity will be valid, \(dU = TdS - pdV\).
See the coffee and bagel problem for a similar problem.
We can zap this with a \(d\) to find that \begin{align} dF &= dU - TdS - SdT \end{align} Keep in mind that, when you zap with \(d\), anything can change, if it is not absolutely and always a constant. Now we need to eliminate the \(dU\), which we can do because we know the thermodynamic identity. \begin{align} dF &= \left(\cancel{TdS}-pdV\right) - \cancel{TdS} - SdT \\ &= -SdT-pdV \end{align} By comparing this to the multivariable chain rule: \begin{align} dF=\left(\frac{\partial F}{\partial T}\right)_V\, dT+\left(\frac{\partial F}{\partial V}\right)_T\, dV \end{align} we can read off the derivative we want: \begin{align} \left(\frac{\partial F}{\partial T}\right)_V &= -S \end{align}