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SR0085076_OWTS
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4200 – Liquid Waste Program
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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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GrencOr <br /> Design <br /> Waste Stream O Primary Treatment Standard AdvanTex Systems <br /> ©Pre-Anoxic Treatment Use for BODS/cBODS,TSS, and Nitrogen Discharge Limits <br /> •See Appendix A for sizing Organic removal is the simplest form of advanced treatment,typically <br /> O Q Standard AdvanTex Treatment requiring only primary and secondary treatment.When loaded at or below <br /> the II g y typ <br /> •Sizing Equations 1.1,1.2 applicable loading rates,standard AdvanTex Treatment Systems i- <br /> cally achieve treatment levels of<10 mg/L BODS/cBODS and TSS(based <br /> Q Pre Anoxic Return Line on 30-day average or 30-day arithmetic mean),and they typically provide <br /> © O reduction of total nitrogen(TN)>60%and removal of ammonia(NH3-N)of <br /> 95%(range 90-99%). <br /> Figure 4 shows the typical configuration for discharge limits associated <br /> with these constituents.See the AdvanTex Unit Sizing section of this <br /> 4 document for the sizing equation listed. <br /> A pre-anoxic stage is recommended for all organic-only removal applica- <br /> Discharge tions and it is required for systems with high-strength primary treated <br /> Figure 4.Treatment Diagram for Removal of Organics effluent(Application Types 5&7). <br /> A two-stage AdvanTex system will be necessary for systems with discharge <br /> limits of NOT TO EXCEED 10 mg/L BODS/cBODS or for discharge limits of <br /> Waste Stream Q Primary Treatment s 5 mg/L BODS/cBODS based on a 30-day average or 30-day arithmetic <br /> mean. <br /> © Pre-Anoxic Treatment <br /> O •See Appendix A for sizing AdvanTex Systems for the Advanced Removal of Nitrogen <br /> Q Standard AdvanTex Treatment Use for Systems with Permits Requiring Discharge Limits of <br /> •Sizing Equations 1.1,1.2,1.3 60-90% Removal of Total Nitrogen,Total Inorganic Nitrogen,or <br /> O QPost-Anoxic Treatment Nitrate Nitrogen <br /> © •Sized at 50%of Maximum For wastewater systems with permit limits for TN,TIN,or NO3-N requiring <br /> Day Design Flow greater than 60% nitrogen reduction,pre-anoxic and post-anoxic treat- <br /> 0 Q Second-Stage ment stages are needed,as well as the possible addition of both supple- <br /> AdvanTex Treatment mental carbon and alkalinity.Figure 5 shows one of the typical configura- <br /> •See Process Stage Section tions for systems with discharge limits requiring this level of treatment. <br /> © for applicability <br /> •Sizing Equations 2.1,2.2,2.3 The nitrification occurring in the AdvanTex treatment stage is heavily influ- <br /> x enced by the alkalinity required to buffer the process(7.14 mg/L alkalinity <br /> o Q oo Qpre-Anoxic Return Line <br /> per 1 mg/L of ammonia-N).pH levels of 7.5 to 8,5 are ideal for complete <br /> Q Alkalinity Feed System nitrification and should be buffered to remain above a pH of 7 for all <br /> p •Two installation options:pre- applications.The use of the pre-anoxic stage benefits overall operation of <br /> anoxic return line or just the system,since denitrification in this stage will return as much as 50% <br /> before Standard AdvanTex of the alkalinity consumed during g nitrification.A supplemental alkalinity <br /> feeder immediately preceding the AdvanTex treatment stage may still be <br /> © Q Carbon Feed System necessary to ensure sufficient alkalinity for nitrification. <br /> •Two options:mix into the <br /> pre-anoxic return line or into Carbon addition should be balanced to the wastewater flows to ensure <br /> Discharge the waste stream just prior carbon-to-nitrogen (C:N) ratios are appropriate. C:N ratios greater than <br /> g to post-anoxic treatment 4:1 are necessary and around 6:1 are preferable,to ensure that denitri- <br /> fication occurs.Carbon is added in the post-anoxic stage to maintain the <br /> Figure 5.Treatment Diagram for Advanced Removal of Nitrogen proper carbon-to-nitrogen ratio.A post—anoxic tank with carbon addition <br /> is generally adequate for applications requiring up to 80%removal of <br /> nitrogen. For applications requiring greater than 80% removal of nitrogen,a moving bed bioreactor(MBBR) is typically necessary.See Post <br /> Anoxic Treatment Stage in the Process Stages—AdvanTex Treatment Systems section for more information. <br /> Depending on permit requirements,either a one-,two-or three-stage configuration is used.When there are stringent organic removal require- <br /> ments(effluent BODS/cBODS<20 mg/L),a two-stage configuration(second stage as polishing) is often used to remove excess carbon(cBODS) <br /> prior to discharge. <br /> NDA-ATX-1 Orenco Systems®•800-348-9843•+1 541-459-4449•www.orenco.com <br /> Rev.8,©10/20 <br /> Page 10 of 38 <br />
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