A simple distillation column is designed to separate an ideal binary mixture to specified distillate and bottoms purities at a given column pressure. If RR$_{\min}$ is the minimum reflux ratio for this separation, select the statement that is NOT CORRECT with regard to the variation in the total annualized cost (TAC) of the column with reflux ratio (RR).
In the design of a distillation column, the reflux ratio (RR) strongly influences both capital cost and operating cost, which together determine the total annualized cost (TAC). As RR increases, the vapor and liquid traffic inside the column increases, leading to larger column diameter and higher energy usage in the reboiler and condenser. Thus, extremely high RR values increase TAC due to higher operating costs. Conversely, when RR approaches RR$_{\min}$, the number of theoretical stages increases sharply, causing a steep rise in the capital cost of the column.
Step 1: Behaviour near RR$_{\min}$
As RR → RR$_{\min}$ from above, the number of stages approaches infinity. This drastically increases column height and capital cost. Therefore, TAC increases sharply near RR$_{\min}$. Hence, option (B) is correct.
Step 2: TAC at intermediate RR
Between RR$_{\min}$ and very high RR, there exists an optimum RR at which TAC is minimized. Option (A) correctly states that TAC has a minimum.
Step 3: TAC at high RR
For RR >> RR$_{\min}$, the column requires a large boil-up rate, increasing utility consumption. This makes TAC rise again, so (D) is correct.
Step 4: Identifying the NOT CORRECT statement
Option (C) states that the "sharpest decrease in TAC occurs as RR approaches RR$_{\min}$ from above," which is incorrect because TAC increases sharply in that region, not decreases. Therefore, (C) is the NOT CORRECT option.
Consider the process in the figure. The liquid-phase elementary reactions \[ A + B \rightarrow P -r_{B1} = k_1 x_A x_B \] \[ P + B \rightarrow S -r_{B2} = k_2 x_P x_B \] \[ S + A \rightarrow 2P -r_{S3} = k_3 x_S x_A \] occur in the continuous stirred tank reactor (CSTR). All fresh feeds, exit streams and recycle streams are pure. At steady state, the net generation of the undesired product $S$ in the CSTR is zero. Let $q = x_A/x_B$ in the reactor. For 90% single-pass conversion of $B$ and fixed product rate, determine the value of $q$ that minimizes the sum of the molar flow rates of the A and S recycle streams (rounded to one decimal place).

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).