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SU0003122
Environmental Health - Public
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EHD Program Facility Records by Street Name
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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
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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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The tank inlet and outlet are level and partially baffled, causing <br /> retention of a portion of the solids. This retention allows the micro- NOTES <br /> organisms to develop large colonies. This simple collection of solids <br /> reduces the overall loading to the aeration reactor and hastens the <br /> process of converting organic nitrogen to ammonium ions. It also <br /> supplies soluble BOD as effluent product/influent wastewater to the <br /> aeration tank. <br /> The lowering of BOD levels in the aeration reactor forces depletion <br /> of available BOD food source in the extended aeration phase. This <br /> enhances the natural dominance of nitrosomonas and nitrobacter <br /> organisms. These organisms predominate and utilize the dead cells <br /> as a carbon source, converting ammonium nitrogen (NH,), as a <br /> nutrient base,to nitrite (NO) through oxidation. <br /> A portion of the resulting nitrate (NO,) rises to the surface of the <br /> reactor and is reduced prior to reaching atmosphere. <br /> The nitrosomonas are responsible for conversion of ammonium ni- <br /> trogen to nitrite, which sponsors the rapid nitrobacter conversion to <br /> nitrate: <br /> NH, + 3/202 —2H + H2O + NO2 (1) <br /> and a portion of the NO2 is then oxidized to NO,: <br /> NO2 + 1/2 02 — NO3 (2) <br /> THE AOUACLEAR PROCESS, DESIGN, AND DESCRIPTION <br /> The AquaClear process concept is derived in part from federal regu- <br /> latory agency guidelines as detailed in Recommended Design Crite- <br /> ria for Activated Sludge Processes. <br /> Raw sewage/wastewater enters the aeration tank, where previously <br /> developed biological floc particles are brought into contact with the <br /> incoming, suspended organic matter. The organic matter is a carbon <br /> and energy source for cell growth and is converted into cell tissue <br /> and oxidized end products(mainly carbon dioxide, CO). <br /> The content of the aeration tank is called mixed liquor (ML). The <br /> biological mass is referred to as the mixed-liquor suspended solids <br /> (MLSS), or mixed-liquor volatile suspended solids (MLVSS), and <br /> consists mainly of microorganisms, inert suspended matter, and non- <br /> biodegradable suspended matter. <br /> After a preset time period, the mixed liquor is transferred to the <br /> clarifier tank for separation of suspended solids from the treated <br /> wastewater. The biological solids are then returned to the aeration <br /> tank to maintain a concentrated population of microorganisms to <br /> treat new, incoming waste. <br /> The use of microprocessor and computer technology has allowed <br /> modifications of the timing cycle which controls the amount of time <br /> 11 <br />
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