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AA BA C D E A <br /> F fl H <br /> REVISION DESCRIPTION I 8Y App DATE <br /> 5 <br /> F <br /> WZ <br /> Q� DESIGN CRITERIA <br /> W� Q W W --7W� a <br /> {n I—Z l 0 cy� ZC} <br /> DESIGN CONDITION <br /> WW, W ��Z FLOW. AWWF, MGD .16 <br /> Q� W Q Q U I—Q �' J Z( FtGW, PwWF, MCD 64 <br /> J J� 8005, mmgg/I 250 <br /> 334 <br /> IL.. ()Q)co SSDSTOTAL,day mg/I 250 <br /> 30 AMMONIA-N, mg/I 25 <br /> O <br /> 25 <br /> q UNIT LOADING, DESIGN PARAMETERS <br /> _ z <br /> q AERATION TANK CAPACITY, MG 1120 <br /> O AERATION RETENTION TIME, ADWF, hours 18 <br /> } 2 0 T CLARIFIER OVERFLOW RATE, ADWF. OPD/sq.ft, 500 <br /> W DIGESTER, % OFSLUDGE AGE. yAERATION TANK 22 <br /> Ij I v v BY-PASS <br /> DECHLORINATION DGESTER-MAXIMUM MLSS, mgll 15000 <br /> 15 DIGESTER-SOLIDS <br /> �ff - - OXYGENTRANSFER RATER %S /5 ,00% <br /> Z F � _MIXED LIQUOR VOLATILEOSUSPENDED SOLIDS, Y.Wt 6117 3 <br /> 10 _ 9.75 F RATIO, LBS. 8045/LF3 MLVSS 0.20 <br /> ZI F/M RATIO, LBS. BOD5/1-8 MLSS 0.13 <br /> Q OVERFLOW 70 EMERGENCY OUTFALL 70 OXYGENCREQUIREMENTS,Ibs 8(Carbonaceousof tl. /I hr. 16ay .46 <br /> I - 5 — STORAGE BASIN HIGHLINE CANAL OXYOEN REQUIREMENTS, (Nitrogenous), mg/I hr. 6.90 <br /> r AER REQUIRED, cfm (Corbonoceous) 261 <br /> Q �.�� ! A REQUIRED, cfm (Nitrogenous) 109 <br /> 0 _ AR REQUIRED, Total cfm 370 <br /> W AIR REQUIRED IN AERATION TANK, cf/Ib of B005/dqy 1599 <br /> W EMERGENCY AUTOMATIC 13Y-PASS MIXED LIQUOR WASTED PER DAY, lbs/dqy 160 <br /> STORAGE POND SLUDGE TO DEWATERING TO EMERGENCY STORAGE MIXED LIQUOR WASTED PER DAY, gallanS/day 6400 <br /> 5 a r_oe iiTY RFT1117?I FACILITIES POND C RETURN DIGESTER SLUDGE AGE, days <br /> mm VOLATILE SOLIDS REDUCTION IN DIGESTER, Y. 31 <br /> SOLIDS WASTED FROM DIGESTER, Ibs/day 130 <br /> _�0 VOLUME WASTED FROM DIGESTER, g011ons/dqy 780 <br /> AIR REQUIRED FOR DIGESTION, cfm 164 <br /> -15 TOTAL PLANT AIR REQUIRED, cfm 534 <br /> FILTER DATA <br /> SURFACE AREA, sq.ft. 38 2 <br /> FILTER RATE AT ADWF, gal/9q.fT./min. 2.9 <br /> REJECT WATER, % of flow 5 <br /> SCHEMATIC FLOW DIAGRAM <br /> AIR REQUIREMENT, D 15-25 pslg 2.3 <br /> DEPTH OF SAND. Inchesch.$ 40 <br /> EXPECTED OVERALL PLANT RESULTS (EFFLUENT) <br /> 8005, MG/L <10 <br /> TOTAL SUSPENDED SOLIDS, MG/L <10 <br /> NITRATES as (N) <10 <br /> COLIFORM, MPN/100 ML <2.2 <br /> AMMONIA (N) MC/L <3 <br /> �o agQf..... q/ 1 <br /> ou`G4 4'o-44 r'. <br /> �^ If0.0 3 =m <br /> THIS DRAWING IS REDUCED `''^—Jg�C/Y/ <br /> s TO HALF SIZE <br /> $ SCALE DATE DE�IONED ERS SUBMITTED FLAG A G C I T Y DRAWING NUMBER SHEET NUMBER <br /> <� AUGusT 1894 ® DE—ANTE AND STOWELL SCHEMATIC FLOW DIAGRAM <br /> _ NQ SCALE FILE DRA1ifN RECDlfIsIMDED CONSULTING ENGINEERS BAN JOAQUIN CG..CAGIroRRiA <br /> off= g3423 CHECKED ERs APPROVED SACRAMENTO.CALIFORNIA WASTEWATER TREATMENT FACILITIES A DESIGN CRITERIA 2 OF 44 <br />