Match the quantities in Group 1 with their units in Group 2
| Group 1 | Group 2 |
|---|---|
| P) Thermal conductivity | I) \( \text{W·m}^{-2}\text{K}^{-1} \) |
| Q) Convective heat transfer coefficient | II) \( \text{W·m}^{-1}\text{K}^{-1} \) |
| R) Stefan-Boltzmann constant | III) \( \text{W·K}^{-1} \) |
| S) Heat capacity rate | IV) \( \text{W·m}^{-2}\text{K}^{-4} \) |
Step 1: Units of thermal conductivity. \[ k: \;\; \frac{\text{W}}{\text{mK}} = \text{Wm}^{-1}\text{K}^{-1}. \] So, \( P \;\rightarrow\; II \).
Step 2: Units of convective heat transfer coefficient. Defined as: \[ q = hA\Delta T. \] Hence, \[ h: \;\; \frac{\text{W}}{\text{m}^2 \text{K}} = \text{Wm}^{-2}\text{K}^{-1}. \] So, \( Q \;\rightarrow\; I \).
Step 3: Units of Stefan–Boltzmann constant. From: \[ q = \sigma T^4, \] we get: \[ \sigma: \;\; \frac{\text{W}}{\text{m}^2 \text{K}^4} = \text{Wm}^{-2}\text{K}^{-4}. \] So, \( R \;\rightarrow\; IV \).
Step 4: Units of heat capacity rate. Defined as: \[ C = \dot m c_p, \] which has units: \[ \frac{\text{J}}{\text{Ks}} = \text{WK}^{-1}. \] So, \( S \;\rightarrow\; III \).
Correct Matching: \[ \boxed{ P \;\rightarrow\; II, \quad Q \;\rightarrow\; I, \quad R \;\rightarrow\; IV, \quad S \;\rightarrow\; III } \] Option (A)
Match the LIST-I with LIST-II
| LIST-I | LIST-II | ||
|---|---|---|---|
| (Type of Fouling) | (Fouling Mechanism) | ||
| A | Precipitation | IV | Precipitation of dissolved substances... |
| B | Freezing | III | Solidification of Liquid components... |
| C | Particulate | I | Accumulation of fine particles suspended... |
| D | Corrosion | II | Heat transfer surface reacts with ambient... |
Identify the evaporator 
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).