The Schmidt number \( Sc \) is a dimensionless quantity used in fluid dynamics to characterize how momentum diffusivity (viscosity) compares to mass diffusivity. It is especially relevant in situations where fluid flow and mass transfer are coupled, such as in chemical reactor design and environmental engineering.
Step 1: Understanding Momentum Diffusivity (Kinematic Viscosity)
Momentum diffusivity, also known as kinematic viscosity \( \nu \), measures the rate at which momentum is diffused within the fluid.
It is typically expressed in \( m^2/s \) and is a fundamental property that describes how viscous a fluid is.
Step 2: Understanding Mass Diffusivity
Mass diffusivity \( D \), on the other hand, measures the rate at which mass is diffused within a fluid.
This property is crucial for describing how species (like solutes in a solvent) spread out over time, also expressed in \( m^2/s \).
Step 3: Ratio of Momentum to Mass Diffusivity
\[
Sc = \frac{\nu}{D}
\]
This ratio, the Schmidt number, tells us how the thickness of the velocity boundary layer compares to the thickness of the mass transfer boundary layer in a fluid flow scenario.
A higher Schmidt number indicates that the momentum boundary layer is thicker than the mass transfer boundary layer, which has implications for the design and operation of equipment where heat and mass transfer processes are significant.
Step 4: Practical Implications
For high Schmidt numbers, momentum diffuses much more slowly than mass.
This is particularly important in gaseous systems where gases have low viscosity.
In liquid systems, where the Schmidt number can be very high, mass transfer operations must be carefully designed to ensure efficient mixing and mass transport.
Consider two identical tanks with a bottom hole of diameter \( d \). One tank is filled with water and the other tank is filled with engine oil. The height of the fluid column \( h \) is the same in both cases. The fluid exit velocity in the two tanks are \( V_1 \) and \( V_2 \). Neglecting all losses, which one of the following options is correct?

A pitot tube connected to a U-tube mercury manometer measures the speed of air flowing in the wind tunnel as shown in the figure below. The density of air is 1.23 kg m\(^{-3}\) while the density of water is 1000 kg m\(^{-3}\). For the manometer reading of \( h = 30 \) mm of mercury, the speed of air in the wind tunnel is _________ m s\(^{-1}\) (rounded off to 1 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).