Consider moist air with absolute humidity of 0.02 (kg moisture)/(kg dry air) at 1 bar pressure. The vapor pressure of water is given by the equation: \[ \ln P_{{sat}} = 12 - \frac{4000}{T - 40} \] where \( P_{{sat}} \) is in bar and \( T \) is in K. The molecular weight of water and dry air are 18 kg/kmol and 29 kg/kmol, respectively. The dew temperature of the moist air is ____________ ℃ (rounded off to the nearest integer).
\[ \ln P_{\text{sat}} = 12 - \frac{4000}{T - 40} \]
Step 2: Calculate the partial pressure of the water vapor:\[ y_{H_2O} = \frac{\text{absolute humidity} \times 1000}{M_{\text{water}}} \times \frac{M_{\text{air}}}{1000} \] \[ y_{H_2O} = \frac{0.02 \times 1000}{18} \times \frac{29}{1000} = 0.0322 \]
The partial pressure of water vapor is:
\[ P_{H_2O} = y_{H_2O} \times P_{\text{total}} = 0.0322 \times 1 = 0.0322 \, \text{bar} \]
Step 3: Solve for the dew temperature \( T \):\[ P_{\text{sat}} = P_{H_2O} = 0.0322 \, \text{bar} \] \[ \ln 0.0322 = 12 - \frac{4000}{T - 40} \] \[ -3.442 = 12 - \frac{4000}{T - 40} \] \[ \frac{4000}{T - 40} = 15.442 \Rightarrow T - 40 = \frac{4000}{15.442} = 259.4 \Rightarrow T = 259.4 + 40 = 299.4 \, K \] \[ T_{\text{dew}} = 299.4 - 273.15 = 26.25^\circ C \]
Therefore, the dew temperature is approximately 26°C.

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).
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, \( V_A = 3V_B \).
A hot plate is placed in contact with a cold plate of a different thermal conductivity as shown in the figure. The initial temperature (at time $t = 0$) of the hot plate and cold plate are $T_h$ and $T_c$, respectively. Assume perfect contact between the plates. Which one of the following is an appropriate boundary condition at the surface $S$ for solving the unsteady state, one-dimensional heat conduction equations for the hot plate and cold plate for $t>0$?
