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SR0085076_OWTS
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4200 – Liquid Waste Program
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SR0085076_OWTS
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Last modified
9/30/2022 4:13:58 PM
Creation date
9/29/2022 9:09:49 AM
Metadata
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Template:
EHD - Public
ProgramCode
4200 – Liquid Waste Program
FileName_PostFix
OWTS
RECORD_ID
SR0085076
PE
4201
FACILITY_NAME
AHERN TRUCK STOP
STREET_NUMBER
29700
Direction
S
STREET_NAME
AHERN
STREET_TYPE
RD
City
TRACY
Zip
95304
APN
25502014
ENTERED_DATE
3/29/2022 12:00:00 AM
SITE_LOCATION
29700 S AHERN RD
P_LOCATION
99
P_DISTRICT
005
QC Status
Approved
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EHD - Public
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11 <br /> Design <br /> For TN,TIN,and NO3-N discharge requirements of<10 mg/L,or for applications with primary treated effluent TN values of>150 mg/L and <br /> >80% nitrogen removal requirements, it will be necessary to integrate a two-stage AdvanTex system,followed by a denitrifying moving bed <br /> bioreactor(MBBRd),denitrification upflow filter,or other denitrification technology into the treatment process. Contact Orenco prior to designing <br /> a system to meet these requirements.See pH Effect on Nitrification and Temperature Effect on Nitrification and Denitrification in the Design <br /> Considerations section on page 19. <br /> Waste Stream O Primary Treatment AdvanTex Systems for the Advanced Removal of Ammonia <br /> Use for Systems with Permits Requiring Discharge Limits > <br /> O Pre-Anoxic Treatment 95% Removal of Ammonia or TKN <br /> •See Appendix A for sizing <br /> O For wastewater systems requiring ammonia removal due to restrictive ammo- <br /> ©Standard AdvanTex Treatment nia nitrogen (NH3 N)or TKN discharge limits(>95%removal),a Second <br /> •Sizing Equations 1.1,1.2,1.3 Stage AdvanTex system will be necessary following standard AdvanTex treat- <br /> 0 Second-stage ment.Figure 6 shows the typical configuration for discharge limits associated <br /> © AdvanTex Treatment with this level of treatment. <br /> •See Process Stage Section The nitrification occurring in the AdvanTex system is heavily influenced <br /> for applicability <br /> O O •Sizing Equations 2.1,2.2,2.3 by the alkalinity required to buffer the process(7.14 mg/L alkalinity per 1 <br /> mg/L of ammonia-N).pH levels of 7.5 to 8.5 are ideal for complete nitri- <br /> fication and should be buffered to remain above a pH of 7 for all applica- <br /> © 0 Alkalinity Feed System tions. Immediately preceding the AdvanTex treatment stage,a supple- <br /> Two installation options;pre- mental alkalinity feeder may be necessary to ensure sufficient alkalinity <br /> anoxic return line or just for nitrification to break down ammonia. <br /> before Standard AdvanTex <br /> 0 Treatment Using a pre-anoxic stage helps buffer pH,as denitrification in this stage <br /> will return as much as 50%of the alkalinity consumed during nitrifica- <br /> tion. In addition, readily available BOD is consumed in the pre-anoxic <br /> denitrification stage, reducing the BOD load to the secondary treatment <br /> Discharge unit. Most application types provide adequate carbon in the incoming <br /> Figure 6.Treatment Diagram for Advanced Removal of Ammonia stream to achieve denitrification and subsequent alkalinity return,but in <br /> the design it is best to ensure that there is enough alkalinity added with- <br /> out relying on this occurrence.As operational data becomes available for the specific treatment system—demonstrating the return of alkalinity <br /> through denitrification—alkalinity feed rates can be adjusted downward.See pH Effect on Nitrification and Temperature Effect on Nitrification and <br /> Denitrification in the Design Considerations section on page 19. <br /> Process Stages — AdvanTex Treatment Systems <br /> Primary Treatment Stage <br /> Purpose and Description: <br /> The primary treatment stage is designed to collect wastewater; segregate settleable and floatable solids(sludge and scum); accumulate,con- <br /> solidate and store solids; digest organic matter; and discharge primary-treated effluent. Passive,energy-free primary tankage provides the most <br /> cost-efficient method of primary treatment available for nonindustrial sewage; BOD removal of>50%and TSS removal of>90% (when using an <br /> effluent filter)are typically accomplished with passive primary treatment. <br /> The primary treatment stage can be configured in several ways, including single- or multiple-compartment tanks,single tanks with meandering <br /> baffles(partitions),or multiple tanks in series.Some systems may utilize solids separation devices. Primary treatment includes effluent screening, <br /> and effluent may be discharged to the secondary treatment stage via gravity or pump. <br /> Design Notes and Special Considerations: <br /> The volume and configuration of primary tankage or inclusion of other primary treatment devices(e.g.solids separation) is dependent on the <br /> system,the application type,and the expected waste strength.When using tankage for primary treatment,proper sizing ensures adequate volume <br /> for the development of the necessary microbial environments,appropriate sludge and scum storage,and surge volume. For recommendations on <br /> sizing of primary tankage,see Appendix A.The tank's structural soundness and watertightness are vital to the system's performance,and all tanks <br /> should be reviewed by the engineer and water-tested in the field after installation. <br /> Orenco Systems°•800-348-9843•+1 541-459-4449•www.orenco.com NDA-ATX-1 <br /> Rev.8,©10/20 <br /> Page 11 of 38 <br />
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