Consider a horizontal rod of radius $aR$ ($a < 1$) in a stationary pipe of radius $R$. The rod is pulled coaxially at a constant velocity $V$ as shown in the figure. The annular region is filled with a Newtonian incompressible fluid of viscosity $\mu$. The steady–state fully–developed axial velocity profile in the fluid is \[ u(r) = V\frac{\ln(r/R)}{\ln(a)}, \] where $r$ is the radial coordinate. Ignoring end effects, the magnitude of the pulling force per unit rod length is

Step 1: Shear stress expression
For a Newtonian fluid, the shear stress is:
\[
\tau_{rz} = \mu \frac{du}{dr}.
\]
We will evaluate this at the rod surface $r = aR$.
Step 2: Differentiate the velocity profile
Given:
\[
u(r) = V\frac{\ln(r/R)}{\ln(a)}.
\]
Differentiate:
\[
\frac{du}{dr} = V\frac{1}{\ln(a)}\frac{d}{dr}[\ln(r/R)]
= V\frac{1}{\ln(a)}\cdot \frac{1}{r}.
\]
Step 3: Evaluate shear at rod surface
At $r = aR$:
\[
\tau_{rz}(aR) = \mu \frac{V}{\ln(a)}\frac{1}{aR}.
\]
Step 4: Force per unit length on rod
The viscous drag per unit length is:
\[
F = \tau \times (\text{surface area per unit length})
= \tau_{rz}(aR) \cdot (2\pi aR).
\]
Substituting:
\[
F = \left(\mu \frac{V}{\ln(a)} \cdot \frac{1}{aR}\right)(2\pi aR)
= \frac{2\pi \mu V}{\ln(a)}.
\]
Step 5: Sign convention
Because $\ln(a)$ is negative for $0 < a < 1$, the expression becomes:
\[
F = \frac{-2\pi \mu V}{|\ln(a)|}.
\]
Thus the force needed to pull the rod is:
\[
F = \frac{-2\pi \mu V}{\ln(a)}.
\]
This exactly matches option (B).
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).