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PROJ00156
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PROJ00156
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Last modified
11/19/2009 11:02:52 AM
Creation date
10/5/2006 11:40:59 PM
Metadata
Fields
Template:
Loan Projects
Contract/PO #
C153721
Contractor Name
Lyons, Town of
Contract Type
Loan
Water District
5
County
Boulder
Loan Projects - Doc Type
Feasibility Study
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<br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br />I <br /> <br />Table 4, Flocculation/Sedimentation Rating Summary <br /> <br />Existing <br /> <br />USEP A CDOH <br />(2) (3) <br />10-40 range 20-30 <br />2- 3 3 <br />10.75 range 10-70 <br />n/a 0,5-2,0 <br /> <br />Flocculation: HDT (minutes) <br />Stages (recommended) <br />Mixing (G Sec -1) <br />Pipe velocities (fPs) <br /> <br />94 (note 1) <br />1 <br />Unknown <br />2,S4 (for 12") <br /> <br />Sedimentation: Surface overflow rate for <br /> <br />Upflow type (g,p,m.lff) LOS <br />Tube settler type (g,p,m.lft2) n/a <br /> <br />0,5-0,7 0,7 <br />1.0-2,0 <br /> <br />n/a <br /> <br />Notes: <br />(1) Computed at 1043 g,p,m, flow rate; 24-hour production of 1,5 MGD, The HDT <br />for the existing basin configuration is a total of 94 minutes, Flocculation HDT is <br />unknown but probably inadequate, <br />(2) Refer to USEPA Handbook, <br />(3) Refer to Colorado Department of Health, Design Criteria, <br /> <br />The duration for which a filter is on-line, called a filter "run", is dependent upon the turbidity <br />of the filter influent. As the production rate through each filter decreases, due to particles <br />entrapped in the filter, water level rises over the filter. The rising level is detected upstream <br />in the clarifier unit; rising levels signal an automated valve to throttle the rate of raw water <br />entering the treatment plant, Chemical addition equipment is similarly adjusted by the <br />operators when production rates are significantly decreased, The operator manually shuts <br />down the plant by closing the influent valve and begins the backwash sequence to clean the <br />filters, At existing peak flow rates of 1043 g,p,m., existing loading rates to the filters are 2,9 <br />g,p,m.lft2, as compared with a maximum rate of 5,0 g,p,m.lft2 as the state criteria, Using the <br />5,0 g,p,m.lft2 rate, the current potential for the filter process is about 2,34 MG/24 hrs, <br /> <br />Detailed review of 1993 operating records and interviews with the operator have revealed that: <br /> <br />19 <br />
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