Step 1: Examine Mass Transfer Theories.
Each mass transfer theory proposes a specific relationship between the mass transfer coefficient \( k \) and the molecular diffusivity \( D_v \), often involving power-law dependencies that reflect the underlying physical phenomena: Film theory generally approximates \( k \) to be proportional to \( D_v^{1/2} \), factoring in the film thickness and diffusivity.
Penetration theory actually suggests \( k \propto D_v^{1/2} \) as well, based on the transient penetration of solute into a stagnant fluid layer. The incorrect statement (B) wrongly attributes \( k \propto D_v^{1/3} \) to Penetration theory.
Surface Renewal theory supports \( k \propto D_v^{1/2} \), consistent with its conceptualization of continuous renewal of surface elements.
Boundary Layer theory correctly describes \( k \propto D_v^{1/2} \) for a laminar boundary layer, again reflecting diffusion across a boundary layer of defined thickness.
Step 2: Identify the Incorrect Statement.
From the theories discussed, the statement (B) incorrectly specifies the relationship for Penetration theory, which should correctly reflect a \( D_v^{1/2} \) dependency, not \( D_v^{1/3} \).
An electrical wire of 2 mm diameter and 5 m length is insulated with a plastic layer of thickness 2 mm and thermal conductivity \( k = 0.1 \) W/(m·K). It is exposed to ambient air at 30°C. For a current of 5 A, the potential drop across the wire is 2 V. The air-side heat transfer coefficient is 20 W/(m²·K). Neglecting the thermal resistance of the wire, the steady-state temperature at the wire-insulation interface __________°C (rounded off to 1 decimal place).

GIVEN:
Kinematic viscosity: \( \nu = 1.0 \times 10^{-6} \, {m}^2/{s} \)
Prandtl number: \( {Pr} = 7.01 \)
Velocity boundary layer thickness: \[ \delta_H = \frac{4.91 x}{\sqrt{x \nu}} \]
The first-order irreversible liquid phase reaction \(A \to B\) occurs inside a constant volume \(V\) isothermal CSTR with the initial steady-state conditions shown in the figure. The gain, in kmol/m³·h, of the transfer function relating the reactor effluent \(A\) concentration \(c_A\) to the inlet flow rate \(F\) is:

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 $t>0$?

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).