2.14 Calculation of \(\mu\) for different models

For virial coefficients as well as for the vdW-equation we will prove some quite fundamental results related to the Joule-Thomson coefficient \(\mu\). The following equation already needs results from the second law of thermodynamics, i.e. the entropy \(S\) is used as well as a Maxwell relation between mixed partial derivatives. So you may take this section as a motivation for discussing the second law, because obviously not all problems can be solved just by conservation of energy.

 \begin{equation*} \begin{split} \mu \;=&\quad \left(\frac{\partial T}{\partial p} \right)_H = - \frac{\left(\frac{\partial H}{\partial p} \right)_T}{\left(\frac{\partial H}{\partial T} \right)_p} \stackrel{1}=\frac{T\,\left(\frac{\partial V}{\partial T} \right)_p-V}{C_p}\stackrel{2}=\frac{V}{C_p}\left(\alpha T - 1 \right)\\ 1\;: \;& \quad - \left(\frac{\partial H}{\partial p} \right)_T = \left(\frac{\partial}{\partial p} \right)_T \left(-T\,dS-V\,dp \right) = - T \left(\frac{\partial S}{\partial p} \right)_T - V = T\, \left(\frac{\partial V}{\partial T} \right)_p -V\\ 2\;:\; & \quad \alpha = \frac{1}{V} \left(\frac{\partial V}{\partial T} \right)_p \quad \mbox{$\alpha$: expansion coefficient.}\\ \end{split} \label{eq:mu_Joule-Thomson} \end{equation*}(2.42)
The expansion coefficient we discussed before in Eq. (2.6). Applying the above equation to different thermal equations of state we find

The Joule-Thomson effect is highly relevant for cooling. Fig. 2.10 shows the Linde process for production of liquid air: The gas must be beneath its inversion temperature (examples for upper inversion temperatures: He: 35 K, H\(_2\): 224 K, N\(_2\): 866 K). The gas cooled by expansion cools compressed gas, further expansion could lead to liquid.


PIC

Figure 2.10: a) scheme of Linde process; b) \(pT\) diagram showing the regimes separated by \(\mu = 0\); c) cooling regime for several gases.



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© J. Carstensen (TD Kin I)