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Water and Wastewater Engineering - Sciences Club

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11-42 WATER AND WASTEWATER ENGINEERING<br />

TABLE 11-9<br />

Design criteria for dual-media filters<br />

Parameter<br />

Reported<br />

range<br />

GLUMRB<br />

recommendation Recommended<br />

Anthracite coal on top<br />

Effective size 0.9–1.4 mm 0.8–1.2 mm<br />

Uniformity coefficient 1.3–1.8 �1.85<br />

Shape factor (f) 0.46–0.73<br />

Porosity 0.53–0.60<br />

Specific gravity 1.45–1.75<br />

Depth of medium<br />

S<strong>and</strong> on bottom<br />

0.4–0.6 m<br />

Effective size 0.35–0.7 mm 0.45–0.55 mm<br />

Uniformity coefficient 1.3–1.8 �1.65<br />

Shape factor (f) 0.7–0.95<br />

Porosity 0.4–0.47<br />

Specific gravity 2.65<br />

Depth of medium 0.3–0.75 m �0.6 m <strong>and</strong> �0.76 m<br />

Filtration rate 7–20 m/h � 15 m/h<br />

Backwash rate 30–60 m/h �24 m/h<br />

Backwash duration a<br />

Surface wash rate<br />

10–20 min �15 min<br />

Revolving arms 1.2–1.8 m/h �1.2 m/h<br />

Fixed arms<br />

Underdrain<br />

4.9–10 m/h �4.9 m/h<br />

Pipe lateral Yes<br />

Block Yes<br />

Air scour No—if total depth of medium<br />

�0.75 m<br />

Air scour 0.6–1.5 m 3 /min · m 2 if total<br />

medium depth � 1 m<br />

a<br />

A ctual off-line time will be � 30 min because of the time required to drain the filter <strong>and</strong> gradually come up to the full<br />

backwash rate. An additional 30–40 minutes off-line is required for “filter-to-waste” to clear the bed of wash water <strong>and</strong><br />

dislodged turbidity. If air scour is provided, the time will be even longer because of the necessity of sequencing the air scour<br />

<strong>and</strong> wash water.<br />

Sources: Castro et al., 2005; Cleasby <strong>and</strong> Logsdon, 1999; GLUMRB, 2003; Kawamura, 2000; MWH, 2005; Reynolds <strong>and</strong><br />

Richardson, 1996.

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