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).
For phase equilibrium, Clausius–Clapeyron relation applies: \[ \frac{d(\ln P^{sat})}{dT} = \frac{\Delta H_{vap}}{RT^2} \] Using two-point approximation: \[ \Delta H_{vap} \approx R \, \frac{\ln(P_2/P_1)}{(1/T_1)-(1/T_2)} \] Substitute values: \[ P_1 = e^{0.693} = 2.00 \text{ bar}, P_2 = e^{1.386} = 4.00 \text{ bar} \] \[ \ln(P_2/P_1) = \ln 2 = 0.693 \] \[ (1/T_1)-(1/T_2) = \frac{1}{350} - \frac{1}{370} \] Compute denominator: \[ \frac{1}{350} - \frac{1}{370} = 0.0001539 \] Thus, \[ \Delta H_{vap} = 8.314 \times \frac{0.693}{0.0001539} \approx 3.63\times10^{4} \text{ J/mol} \] \[ \Delta H_{vap} \approx 36.3 \text{ to } 38.3 \text{ kJ/mol} \]
An ideal monoatomic gas is contained inside a cylinder-piston assembly connected to a Hookean spring as shown in the figure. The piston is frictionless and massless. The spring constant is 10 kN/m. At the initial equilibrium state (shown in the figure), the spring is unstretched. The gas is expanded reversibly by adding 362.5 J of heat. At the final equilibrium state, the piston presses against the stoppers. Neglecting the heat loss to the surroundings, the final equilibrium temperature of the gas is __________ K (rounded off to the nearest integer).
The residence-time distribution (RTD) function of a reactor (in min$^{-1}$) is 
The mean residence time of the reactor is __________ min (rounded off to 2 decimal places).}
Ideal nonreacting gases A and B are contained inside a perfectly insulated chamber, separated by a thin partition, as shown in the figure. The partition is removed, and the two gases mix till final equilibrium is reached. The change in total entropy for the process is _________J/K (rounded off to 1 decimal place).
Given: Universal gas constant \( R = 8.314 \) J/(mol K), \( T_A = T_B = 273 \) K, \( P_A = P_B = 1 \) atm, \( V_B = 22.4 \) L, \( V_A = 3V_B \).
The following data is given for a ternary \(ABC\) gas mixture at 12 MPa and 308 K:
\(y_i\): mole fraction of component \(i\) in the gas mixture
\(\hat{\phi}_i\): fugacity coefficient of component \(i\) in the gas mixture at 12 MPa and 308 K
The fugacity of the gas mixture is __________ MPa (rounded off to 3 decimal places).