For a single component system at vapor-liquid equilibrium, the extensive variables A, V, S and N denote the Helmholtz free energy, volume, entropy, and number of moles, respectively, in a given phase. If superscripts \( (\nu) \) and \( (\ell) \) denote the vapor and liquid phase, respectively, the relation that is NOT CORRECT is
Step 1: Analyze the relations.
The first three options (A), (B), and (C) are correct relations derived from thermodynamic identities. However, option (D) is not correct because the relation \( \left( \frac{A + TS}{N} \right)^{(\ell)} = \left( \frac{A + TS}{N} \right)^{(\nu)} \) is not valid for a general vapor-liquid system, as the specific values of \( A \), \( T \), and \( S \) differ between the liquid and vapor phases.
Step 2: Conclusion.
The relation in option (D) is not correct. Hence, the correct answer is (D).
Final Answer: (D) \( \left( \frac{A + TS}{N} \right)^{(\ell)} = \left( \frac{A + TS}{N} \right)^{(\nu)} \)

For a pure substance, the following data at saturated conditions are given:
\[ \begin{array}{c c} \ln P^{sat} \, (\text{bar}) & T \,(\text{K})\\ 0.693 & 350\\ 1.386 & 370 \end{array} \] Assume the vapor behaves ideally, liquid molar volume is negligible, and latent heat of vaporization is constant over this range. The universal gas constant is $R=8.314$ J mol$^{-1}$ K$^{-1}$. From the above data, the estimated latent heat of vaporization at 360 K is \(\underline{\hspace{2cm}}\) kJ/mol (rounded to one decimal place).