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.
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: \[ \delta_H = \frac{4.91 x}{\sqrt{x \nu}} \]
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?
Choose the option that correctly matches the items in Group 1 with those in Group 2.
Consider a process with transfer function: \[ G_p = \frac{2e^{-s}}{(5s + 1)^2} \] A first-order plus dead time (FOPDT) model is to be fitted to the unit step process reaction curve (PRC) by applying the maximum slope method. Let \( \tau_m \) and \( \theta_m \) denote the time constant and dead time, respectively, of the fitted FOPDT model. The value of \( \frac{\tau_m}{\theta_m} \) is __________ (rounded off to 2 decimal places).
Given: For \( G = \frac{1}{(\tau s + 1)^2} \), the unit step output response is: \[ y(t) = 1 - \left(1 + \frac{t}{\tau}\right)e^{-t/\tau} \] The first and second derivatives of \( y(t) \) are: \[ \frac{dy(t)}{dt} = \frac{t}{\tau^2} e^{-t/\tau} \] \[ \frac{d^2y(t)}{dt^2} = \frac{1}{\tau^2} \left(1 - \frac{t}{\tau}\right) e^{-t/\tau} \]
Is there any good show __________ television tonight? Select the most appropriate option to complete the above sentence.