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SU0002246 SSNL
Environmental Health - Public
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SU0002246 SSNL
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Entry Properties
Last modified
5/7/2020 11:29:08 AM
Creation date
9/5/2019 11:00:06 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
FileName_PostFix
SSNL
RECORD_ID
SU0002246
PE
2626
FACILITY_NAME
UP-98-18
STREET_NUMBER
16450
Direction
E
STREET_NAME
HARNEY
STREET_TYPE
LN
City
LODI
Zip
95240
ENTERED_DATE
10/26/2001 12:00:00 AM
SITE_LOCATION
16450 E HARNEY LN
QC Status
Approved
Scanner
SJGOV\rtan
Supplemental fields
FilePath
\MIGRATIONS\H\HARNEY\16450\UP-98-18\SU0002246\NL STDY.PDF
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EHD - Public
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Technical Description <br /> Oxygen is essential for the growth of nitrifiers, and alkalinity consumption is important because <br /> nitrifying organisms are efficient only over a relatively narrow pH range. The third parameter, <br /> biomass production, is important to the understanding of microbial population dynamics. <br /> The low cell production frequently causes washout of nitrifiers in combined carbon-nitrogen oxi- <br /> dation systems without high sludge age. The Nitro-Raptor batch process assures that washout is <br /> less likely to occur than in a conventional flowthrough system or process due to the design of the <br /> hydraulic control. <br /> Compared to heterotrophic oxidation of carbonaceous waste material, nitrification generates rela- <br /> tively little biomass. Therefore, additional solids capacity for nitrogenous processing beyond <br /> those allocations given for the heterotrophic process is not required. <br /> The Nitro-Raptor batch system removes an average 96.8%of nitrates. <br /> (NOTE.•By increasing detention time from 14 to 16 hours,the process begins to run out the right <br /> side of the growth curve. This additional detention time utilizes Oz demand for further conver- <br /> sion of NH,to NO3.) <br /> Samples of MLSS are pulled from the ML entering the clarifier. <br /> Formula: <br /> F:M = Influent BOD, lbs/dav (6) <br /> Solids in aeration, lbs <br /> Example: Calculate the F:M_ <br /> _ Assumptions: <br /> Q=0.075 MGD <br /> Aeration tank volume,V=0.050 MGD <br /> BOD; = 125 mg/L <br /> MLVSS = 1600 mg/L <br /> F = Influent BOD 5 <br /> = (BODS)(Q,MGD) (8.34 lbslry <br /> (125)(0.075)(8.34) <br /> 78.18 lbs/day <br /> m = Solids inventory in aeration tank <br /> = MLVDD mg/L)(V, MGD) (8.34 lbs/gal) <br /> = (1600) (0.050) (8.34) <br /> = 667.2 lbs <br /> F:M = 78.18 BODJday <br /> 667.2 lbs MLVSS <br /> = 0.11 lbs BODS/day/lb MLVSS <br /> Extended aeration detention sizing: <br /> Fxh = C <br /> H1 <br /> where <br /> - ts <br /> 7-H Technical Services Group,Inc. <br />
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