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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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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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i <br /> Technical Description <br /> ff <br /> Characteristics ofthe activated sludge play an important part in this settling time.A good food source, <br /> along with adequate oxygen, produces a fluffy bacteria. It is these light, fluffy bacteria that produce <br /> the floccing action in the clarifier. Because both the food source and oxygen are depleted in the <br /> clarifier, the sludge loses its fluffiness and is pulled down by gravity, leaving a visible separation <br /> ' between the supernatant, or clarified, liquid and the sludge. <br /> If the SSV-60 test indicates sludge-wasting is required, the following procedure should be used: <br /> After the supernatant has been transferred from the clarifier, 5% percent of the remaining sludge, <br /> which has no odor, may be returned to the buffer tank, discharged for direct drying on open beds, <br /> diverted to an optional sludge digester, or accumulated for disposal in designated areas. <br /> - Bio-Pure system will batch 6 494 gallons of mixed liquor to the clarifier <br /> EXAMPLE: A 30,000 gpd B o y , g q <br /> from the aeration chamber.After a 60-minute settling period in the clarifier,2,164 gallons of the batch <br /> are removed as supernatant and the remaining 4,329 gallons are classified as sludge. A minimum of <br /> five percent of the sludge, or 217 gallons, would be wasted. <br /> This wasting procedure follows recommendations described in Operation of Waste Treatment <br /> Plants published by California State University, Sacramento, Department of Civil Engineering, in <br /> cooperation with the California Water Pollution Control Association for the Federal Environmental <br /> Protection Agency, Office of Water Program Operations. <br /> Bio-Pure systems have a field history of extremely low sludge generation and will probably not require <br /> sludge-wasting at all during the first 12 to 18 months of plant operation. After that period, wasting <br /> may be required as indicated by the SSV;60 test, normally about once each month. Remember that <br /> sludge generation is always a function of influent characteristics, treatment system design, collection <br /> t system integrity, and operator skills, with emphasis on operator skills. <br /> The Bio-Pure process, when compared to a flowthrough system,will produce a much higher quality <br /> effluent with far less sludge production. :! <br /> a <br /> The Bio-Pure process concept is covered, in part, in federal regulatory agency guidelines as detailed <br /> in Recommended Design Criteria for Activated Sludge Processes. <br /> The Bio-Pure batch reactor process is a modified version of the activated- <br /> sludge process. Known as <br /> a complete-mix system, it treats wastewater in batches, sequentially controlled by a microprocessor <br /> timing system. This unique feature makes possible effective, quality treatment of sewage, regardless <br /> of input surge-flow patterns. The principal steps are:. <br /> Raw sewage/wastewater enters the aeration tank,'where previously developed biological floc <br /> particles are brought into contact with the incoming, suspended organic matter. The organic matter <br /> is a carbon and energy source for cell growth and is converted into cell tissue and/or completely <br /> converted to carbon dioxide (CO2). <br /> The digestion process in the aeration chamber is initiated by the introduction of air into the incoming <br /> wastewater. The soluble material, oxidized material, settleable and suspended solids form the mixed <br />' liquor. This biological mass is referred to as the mixed liquor suspended solids (MI-.SS), or mixed <br /> 5 <br />
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