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SU0005897 SSNL
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SU0005897 SSNL
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Last modified
5/7/2020 11:31:51 AM
Creation date
9/6/2019 10:03:52 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
FileName_PostFix
SSNL
RECORD_ID
SU0005897
PE
2691
FACILITY_NAME
PA-0600037
STREET_NUMBER
11293
Direction
S
STREET_NAME
MANTHEY
STREET_TYPE
RD
City
LATHROP
Zip
95330
APN
19125008
ENTERED_DATE
1/31/2006 12:00:00 AM
SITE_LOCATION
11293 S MANTHEY RD
RECEIVED_DATE
1/31/2006 12:00:00 AM
P_LOCATION
99
P_DISTRICT
003
QC Status
Approved
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SJGOV\rtan
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\MIGRATIONS\M\MANTHEY\11293\PA-0600037\SU0005897\NL STDY.PDF
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EHD - Public
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C75.5Calculation of Alkalinity Requirement for Nitrification <br /> All of the nitrate-nitrogen loading calculations above are contingent upon the environmental <br /> factors required for nitrification to occur. These conditions include soil pore-space oxygen content, <br /> soil temperature, pH, electrical conductivity, organic matter, cation exchange capacity, and <br /> alkalinity. Alkalinity in wastewater effluent is derived from the domestic water supply in addition <br /> to the introduction of wastes. As referenced,nitrification consumes approximately 7.1 mg of <br /> alkalinity for every milligram of ammonia-nitrogen (NH4-I) oxidized. Effluent sampled from <br /> domestic and commercial septic tanks typically exhibit higher alkalinity than groundwater, with <br /> domestic well water from deeper aquifers generally having a much lower alkalinity than shallower <br /> groundwater from shallow wells. <br /> Nitrification of the average Total Nitrogen concentration of 87 mg/L as used in the calculations <br /> would require the following: Assume that of the 87 mg/L Total Nitrogen, 70% is in the ammonium <br /> form: 87 x 70%= 61 NH4 N x 7.1 mg CaCO3 =432 mg/L alkalinity. As noted in Table 6, the J <br /> alkalinity from the domestic well was 220 mg/L. Consequently, the anticipated wastewater must <br /> contribute approximately 210 mg/L of alkalinity for nitrification to readily proceed. <br /> 6. PRELIMINARY WASTEWATER DISPOSAL OPERATIONAL CRITERIA <br /> The following information describes the preliminary details of the wastewater disposal system for <br /> the different types of commercial business within the subject complex. Since the entire project is in <br /> the initial phases of planning, several facets of the project are subject to change;which in tum would <br /> cause changes to the wastewater disposal system ultimately installed. <br /> Septic and Grease Interceptor Tanks <br /> SSS§3.7 Influent from each of the different business within the Complex must flow either by <br /> gravity or low pressure piping systems into septic tanks. Food wastes from the restaurants must <br /> flow into interceptor tanks, commonly referred to as grease traps. These tanks will provide the <br /> preliminary treatment of the influent from all of the businesses. The volume of tanks required is <br /> primarily dependant upon hydraulic residence time, although other factors may also be considered <br /> on a site-specific basis. <br /> 1 6.2 Septic Tank Volume Hydraulic Detention Time Example - Completely Built Out <br /> j Project Consisting of both Phase 1 and Phase 2 <br /> Detention Time=70,000 gal septic tank capacity x 0.70 (30%volume lost to sludge/scum accumulation) <br /> 2 (Peaking Factor) x 25,830 gals/day <br /> Detention Time= 1.0 day. The minimum acceptable detention time is 1.0 day. <br /> Septic Tank Volume Hydraulic Detention Time Example - Phase 1 Exclusively <br /> 1 Detention Time= 35,00 gal septic tank capacity x 0.70 (30%volume lost to sludge/scum accumulation) <br /> 2 (Peaking Factor) x 12,000 gals/day <br /> Detention Time = 1.0 day. <br /> Page -22- <br /> Chesney Consulting <br />
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