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Science of Water : Concepts and Applications

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382 The <strong>Science</strong> <strong>of</strong> <strong>Water</strong>: <strong>Concepts</strong> <strong>and</strong> <strong>Applications</strong><br />

Step 3. Compute total head loss.<br />

h 0.0410 m0.5579 m<br />

0.599 m<br />

HEAD LOSS THROUGH A FLUIDIZED BED<br />

If the upward water fl ow rate through a fi lter bed is very large the bed mobilizes pneumatically<br />

<strong>and</strong> may be swept out <strong>of</strong> the process vessel. At an intermediate fl ow rate the bed exp<strong>and</strong>s <strong>and</strong> is<br />

in what we call an exp<strong>and</strong>ed state. In the fi xed bed the particles are in direct contact with one<br />

another, supporting one another’s weight. In the exp<strong>and</strong>ed bed, the particles have a mean free<br />

distance between particles <strong>and</strong> the drag force <strong>of</strong> the water supports the particles. The exp<strong>and</strong>ed<br />

bed has some <strong>of</strong> the properties <strong>of</strong> the water (i.e., <strong>of</strong> a fl uid) <strong>and</strong> is called a fl uidized bed (Chase,<br />

2002). Simply, fl u i d i z a t i o n is defi ned as upward fl ow through a granular fi lter bed at suffi cient<br />

velocity to suspend the grains in the water. Minimum fl uidizing velocity (Umf ) is the superfi cial<br />

fl uid velocity needed to start fl uidization; it is important in determining the required minimum<br />

backwashing fl ow rate. Wen <strong>and</strong> Yu proposed the Umf equation including the near constants (over<br />

a wide rang <strong>of</strong> particles) 33.7 <strong>and</strong> 0.0408, but excluding porosity <strong>of</strong> fl uidization <strong>and</strong> shape factor<br />

(Wen <strong>and</strong> Yu, 1966):<br />

U<br />

mf<br />

05 . 33. 7<br />

( 1135. 690. 0408Gn)<br />

<br />

pd<br />

pd<br />

where<br />

µ = absolute viscosity <strong>of</strong> water, N s/m 2 or lb s/ft 2<br />

p = density <strong>of</strong> water, kg/m 3 or lb/ft 3<br />

d eq = d 90 sieve size is used instead <strong>of</strong> d eq<br />

G n = Galileo number<br />

eq<br />

eq<br />

(10.84)<br />

3<br />

2<br />

Gndeqp( ps − p) g<br />

(10.85)<br />

Other variables used are expressed in Equation 10.83.<br />

√ Note: Based on the studies <strong>of</strong> Cleasby <strong>and</strong> Fan (1981), we use a safety factor <strong>of</strong> 1.3 to ensure<br />

adequate movement <strong>of</strong> the grains.<br />

Example 10.100<br />

Problem:<br />

Estimate the minimum fl uidized velocity <strong>and</strong> backwash rate for the s<strong>and</strong> fi lter. The d90 size <strong>of</strong> s<strong>and</strong> is<br />

0.90 mm. The density <strong>of</strong> s<strong>and</strong> is 2.68 g/cm3 .<br />

Solution:<br />

Step 1. Compute the Galileo number.<br />

From given data <strong>and</strong> the applicable table, at 15°C:<br />

p = 0.999 g/cm3 µ = 0.0113 N s/m2 = 0.00113 kg/ms = 0.0113 g/cm s<br />

µp = 0.0113 cm2 /s

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