Flow through Packed Bed
Apparatus required :
CCL4 manometer, Hg manometer.
Procedure :
- Keep the bypass valve completely open and the main valve completely closed. Switch on the pump.
- Connect a CCL4 manometer across the packed bed. Open the main valve and allow the fluid to flow through the bed.
- Wait till steady state is attained
- Note down the manometer reading and the flow rate using the rotameter.
- Increase the flow rate by opening the main valve and throttling the bypass valve suitably and repeat steps (3) and (4).
- Use Hg manometer at higher flow rates.
- After completing the experiment, close the main valve. Switch off the pump. Determine the void volume by draining water from the column.
Data :
Nominal pipe(column) diameter =
Actual pipe(column) diameter = D = m
Length of the packed bed = L = m
Density of fluid = = kg/m3
Viscosity of fluid= = cp
Density of CCL4 = CCL4 = kg/m3
Density of Hg = Hg= kg/m3
Observations :
Volume of voids = m3
= Sphericity =
Specific surface area = S = m2/m3= surface area/Unit bed area

Calculations :
Flow rate:
Pressure drop in cm of manometric fluid =
Bed Porosity = = void volume/volume of bed
Cross sectional area of the bed = = m2
Volume of bed = *L=m3
Equivalent diameter of the particles, Dp=6(1-)/
*S= m
Mass flow rate = = Volumetric flowrate * density
Superficial mass velocity, G0=/cross sectionalarea of tower= kg/s.m2
m
and
are density of manometric fluid and density of fluid .
= N/m2
Modified Reynolds number,
NRep=Dp*G0/
= viscosity of fluid

Plot
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Find the slope = n
Then
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Calculate Modified friction factor

Verify Ergun's Equation given below
Plot fpvs 1/NRep on an ordinary graph sheet. Find the slope and intercept.
Check for the validity of Ergun's equation

plot ftheo vs NRep on a log-log graph.
Results :
Comment on effect of modified Reynolds number on modified friction factor. Comment on effect of superficial mass velocity on process drop across the bed and report n.