For a shell-and-tube heat exchanger, the clean overall heat transfer coefficient is calculated as 250 W m$^{-2}$ K$^{-1}$ for a specific process condition. It is expected that the heat exchanger may be fouled during the operation, and a fouling resistance of 0.001 m$^{2}$ K W$^{-1}$ is prescribed. The dirt overall heat transfer coefficient is \(\underline{\hspace{2cm}}\) W m$^{-2}$ K$^{-1}$.
Step 1: Compute clean thermal resistance.
\[
\frac{1}{U_{\text{clean}}} = \frac{1}{250} = 0.004 \; \text{m}^2 \text{K W}^{-1}.
\]
Step 2: Add fouling resistance.
Fouling resistance = 0.001 m$^2$ K W$^{-1}$.
\[
R_{\text{total}} = 0.004 + 0.001 = 0.005.
\]
Step 3: Compute dirty overall heat transfer coefficient.
\[
U_{\text{dirty}} = \frac{1}{R_{\text{total}}}
= \frac{1}{0.005}
= 200 \; \text{W m}^{-2} \text{K}^{-1}.
\]
Thus, the dirt overall heat transfer coefficient is 200 W m⁻² K⁻¹.
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).