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SU0003122
Environmental Health - Public
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THORNTON
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2600 - Land Use Program
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SA-93-26
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SU0003122
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Entry Properties
Last modified
5/7/2020 11:29:41 AM
Creation date
9/9/2019 10:38:07 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
RECORD_ID
SU0003122
PE
2633
FACILITY_NAME
SA-93-26
STREET_NUMBER
26440
Direction
N
STREET_NAME
THORNTON
STREET_TYPE
RD
City
THORNTON
ENTERED_DATE
11/6/2001 12:00:00 AM
SITE_LOCATION
26440 N THORNTON RD
QC Status
Approved
Scanner
SJGOV\rtan
Supplemental fields
FilePath
\MIGRATIONS\T\THORNTON\26440\SA-93-26\SU0003122\APPL.PDF \MIGRATIONS\T\THORNTON\26440\SA-93-26\SU0003122\CDD OK.PDF \MIGRATIONS\T\THORNTON\26440\SA-93-26\SU0003122\EH COND.PDF \MIGRATIONS\T\THORNTON\26440\SA-93-26\SU0003122\CORRESPOND.PDF
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EHD - Public
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Description of the "Batch" Process <br /> The BIO-PURE® treatment system utilizes an aerobic process which provides both extended aera- <br /> tion and contact stabilization.All waste liquor passes successively through four stages for secondary <br /> treatment and five for tertiary treatment: <br /> Secondary Tertiary <br /> 1. Disintegration 1. Disintegration <br /> 2. Aeration 2. Aeration <br /> 3. Clarification 3. Clarification <br /> 4. Disinfection (Chlorination) 4. Disinfection (CL,, or U.V.) <br /> 5. Filtration <br /> The secondary process is shown in the following diagram: <br /> S <br /> RAW EWAGE TREATED�SECONDARY <br /> WIENINFLUENT <br /> Of <br /> ` I L <br /> 0 HIGH LEVEL , <br /> PL flM L <br /> C-[ <br /> T' <br /> 9DREEN 1 <br /> OSTANDBY <br /> LEVEL <br /> MIXED LIDUOR <br /> TRANSFER PUMP <br /> DISCHARGE PUMP <br /> AERATION CHLORINE RETURN <br /> PUMPjLnPUMP <br /> AERATION CHAMBER CLARIFIER CLi CONTACT CHAMBER <br /> The BIO-PURE® batch process is programmed through tact chamber is pressure discharge to the filters or the <br /> a Solid State Controller to provide consistent treatment receiving body, the remaining liquid in the chamber is <br /> regardless of the erratic flows encountered from domestic returned to the aeration chamber for further biological <br /> wastewater systems. The turbulent action of air flow treatment. <br /> directed at the bottom of the Disintegrator Basket results <br /> in the attrition of all degradable solids entering the plant. The chlorine contact chamber is now ready to receive the <br /> After passing through the disintegrator all influent collects clarified supernatant. Chlorination is accomplished by <br /> in the aeration chamber where it is mixed with biologically pumping the supernatant through a non-mechanical, <br /> active mixed liquor and is digested.The Aeration Chamber splitflow chlorinator.Chlorine contact time is approximate- <br /> remains at least one-fourth full at all times in order to pro- ly seventy minutes. On completion of the supernatant <br /> vide a basic colony of bacteria for digestion fresh influent. transfer, the remaining liquid and sludge is pumped back <br /> The Aeration Chamber also provides a surge tank for to the Aeration Chamber for further treatment by the <br /> variable influent flow rates. bacteria. <br /> As the level in the Aeration Chamber raises to the Stand- In applications where Ultra Violet disinfection is desired <br /> by Level float switch, this starts the Controller and Mixed the pressure effluent is transferred through the dual media <br /> Liquor is transferred to the clarifier and accompanied by filters and into the LIM unit. Once passing through the <br /> a minimum two minute automatic skimming of floatable U.V. the disinfected effluent enters the outfall. <br /> solids back to the Aeration Chamber. Quiescent settling <br /> takes place for a minimum of sixty minutes. Prior to the Filter backwash can either be directed into the Aeration <br /> transfer of the Settled supernatant liquor, approximately Chamber or into a BIO-PURE® packaged Digester. <br /> ninety five percent of the treated water in the chlorine con- <br />
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