Step 1: Understand the Kozeny-Carman equation and its applications.
The Kozeny-Carman equation is a relationship that describes the flow of a fluid through a packed bed of solids. It is derived from a simplified model of fluid flow through a porous medium, assuming laminar flow conditions. The equation relates the pressure drop across the packed bed to the fluid velocity, fluid viscosity, bed porosity, particle size, and bed length.
The general form of the Kozeny-Carman equation for pressure drop (\(\Delta P\)) is often expressed as: $$\frac{\Delta P}{L} = \frac{\mu v_s}{k}$$ Where:
\(\Delta P\) is the pressure drop across the bed.
\(L\) is the length of the packed bed.
\(\mu\) is the dynamic viscosity of the fluid.
\(v_s\) is the superficial velocity of the fluid (flow rate divided by the cross-sectional area of the bed).
\(k\) is the permeability of the packed bed, which is related to the properties of the solid particles and the porosity of the bed.
A more detailed form of the permeability \(k\) based on the Kozeny-Carman theory is: $$k = \frac{\epsilon^3}{c (1-\epsilon)^2 S_p^2}$$ Where:
\(\epsilon\) is the porosity of the packed bed (void volume fraction).
\(c\) is the Kozeny constant or Kozeny factor, which depends on the shape and orientation of the particles (typically around 5 for randomly packed beds of spheres).
\(S_p\) is the specific surface area of the particles per unit volume of solids.
Substituting this permeability into the pressure drop equation shows that the Kozeny-Carman equation is fundamentally used to determine the pressure drop associated with fluid flow through a packed bed.
Step 2: Evaluate the given options based on the understanding of the Kozeny-Carman equation.
(1) Volumetric flow rate through a pipe line: The Kozeny-Carman equation is specifically for flow through porous media like packed beds, not open conduits like pipelines. The Hagen-Poiseuille equation or Darcy-Weisbach equation are more relevant for flow in pipes. (2) Velocity of fluids through a duct: While the Kozeny-Carman equation involves fluid velocity (superficial velocity), its primary purpose is not to directly find the velocity in a general duct but to relate it to the pressure drop in a packed bed. (3) Pressure drop through a packed bed: As discussed in Step 1, the Kozeny-Carman equation directly relates the pressure drop across a packed bed to the fluid and bed properties. This is the primary application of the equation. (4) Pressure drop through a fluidized bed: A fluidized bed is a different regime of fluid-solid interaction compared to a packed bed. In a fluidized bed, the solid particles are suspended in the fluid, and the flow characteristics and pressure drop relationships are different from those in a static packed bed described by the Kozeny-Carman equation. The Ergun equation is often used for pressure drop in fluidized beds, as it covers a wider range of flow rates, including the transition to fluidization.
Step 3: Conclude the correct application of the Kozeny-Carman equation.
Based on the analysis, the Kozeny-Carman equation is used for finding the pressure drop through a packed bed.
A negligibly thin horizontal plate PQ has a length 3 m and width 1 m. It is being pulled along its length at a speed of 1 m/s in between two static parallel plates as shown in the figure. The gap of 6 cm between the plates is filled with a Newtonian fluid of dynamic viscosity \( \mu = 0.2 \, {N-s/m}^2 \). The thin plate is located at 3 cm from the top surface. The velocity distribution between the thin plate and the static plates is linear.
The steady force required to pull the plate is __________ N (answer in integer).
The representation of octal number \((532.2){_8}\) in decimal is ____ .
Given the signal,
\(X(t) = cos t\), if \(t<0 \)
\(Sin\ t\), if \(t\ge0 \)
The correct statement among the following is?
A linear system at rest is subject to an input signal \(r(t) = 1 - e^{-t}\). The response of the system for t>0 is given by \(c(t) = 1 - e^{-2t}\). The transfer function of the system is:
In the given circuit below, voltage \(V_C(t)\) is: