MIXING FORMULAE

                       FOR

         ACTIVATED SLUDGE CHARACTERISTICS
                    ADAPTED BY

                 A. W. West, P.E.
           Chief, Sewage Treatment Plant
             Operations & Design Branch
          ENVIRONMENTAL PROTECTION AGENCY
               WATER QUALITY OFFICE
    OFFICE OF ENFORCEMENT & STANDARDS COMPLIANCE
DIVISION OF FIELD INVESTIGATIONS - CINCINNATI  CENTER
                    APRIL 1971

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33IVIRONMENTAL PROTECTION AGENCY

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                                                 305R71101
                     MIXING FORMULAE
             FOR ACTIVATED SLUDGE CALCULATIONS
                      CASE A
                                     CASE B
                   General - When
               Significant Amounts of
                Solids are drawn out
              in the Clarifier Effluent
                                 Usual Practice
                                   with Clear
                                Clarifier Effluents
                                     (FEC   o)
CSP
       ATC - FEC
       RSC - ATC
                                                      ATC
                                                   RSC - ATC
RSC
     ATC +
ATG - FEC
   CSP
ATC
ATC
CSP
ATC
    (CSP x RSC) + FEG
        CSP +  1.0
                          CSP x RSC
                          CSP -t- 1.0
                                   EXAMPLES
CSP
RSC
ATC
3.2
WHEN
ATC = 3-2
RSC =10.7
FEC = 0.2
(CSP = O.UO)
3'2 - °'2 o ho
10.7 - 3.2 - U>4U
- , 3.2 - 0.2
| .„_.„ .JM.n. JJJ f f(J
x 10.7) + 0.2 _ pn
WHEN
ATC = 3-
RSC = 11.
FEC = 0.
(CSP = 0.
3.2
11.2 - 3-2
3-2 + Si)-
O.U x 11.2

2
2
0
k(



                                                20
                                               *  °

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                ABBREVIATIONS
                     for
               MIXING FORMULAE

FLOWS    (WASTE WATERS, MIXED LIQUOR, & EFFLUENT)
 PFO         PRIMARY GIARIFIER FLOW (OUT OF)
 TFO         SLUDGE THICKENER FLOW (OUT OF)
 AFI         AERATOR FLOW (WASTE WATER I_N)
 TFL         TOTAL FLOW (OUT OF AERATOR)
 CFI         FINAL GIARIFIER FLOW (IN TO)
 GFO         FINAL CLARIFIER FLOW (OUT OF)
SLUDGE FLOWS
 CSF         FINAL CIARIFIER SLUDGE FLOW
 RSF         RETURN SLUDGE FLOW
 XMF         EXCESS MIXED LIQUOR FLOW TO WASTE
 XRF         EXCESS RETURN SLUDGE FLOW TO WASTE
 CSP         CIARIFIER SLUDGE FLOW PERCENT OF CFO
CONCENTRATIONS ($ by CENTRIFUGE)
 ATC         AERATION TANK CONCENTRATION(MIXED LIQUOR)
 RSC         RETURN SLUDGE CONCENTRATION
 FEC         FINAL EFFLUENT CONCENTRATION(EQUIV.  CENTR.)

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                  CHECK MIXING FORMULAE BY MASS BALANCE
        CUT A SECTION AROUND THE FINAL CLARIFIER, AND THE SIUDGE
        UNITS COMING OUT MUST EQUAL (OR APPROXIMATE IN ACTUAL
        PRACTICE) THE SLUDGE UNITS ENTERING THE CLARIFIER.
             1)     ONE SLUDGE UNIT (SLU) IS DEFINED AS THE AMOUNT
                    OF SLUDGE IN ONE GALLON AT A ONE PERCENT CON-
                    CENTRATION (EXPRESSED AS A DECIMAL) BY CENTRI-
                    FUGE, i.e., 10.0 mg at 4.0$ by CENTRIFUGE =
                    10 x 0.04 = 0.40 MILLION SLUDGE UNITS.

             2)     THE EQUIVALENT CENTRIFUGE CONCENTRATION OF LOW
                    LEVEL SOLIDS IN CLARIFIER EFFLUENTS CAN BE CAL-
                    CULATED FROM THE MEASURED TSS AND THE DAILY
                    MLTSS/ATC RATIO.

                    i.e., IF THE MIXED LIQUOR CONCENTRATED TO 4.2$
                    IN THE CENTRIFUGE, AND MEASURED 3360 mg/1 by
                    WEIGHT: - THE MLTSS/ATC RATIO = 3360/4.2 = 800.

                    THEN IF THE CLARIFIER EFFLUENT CONTAINED SOLIDS
                    CONCENTRATIONS BELOW THE RANGE FOR ACCURATE
                    CENTRIFUGE DETERMINATIONS, - THE EQUIVALENT
                    CENTRIFUGE CONCENTRATION IS: -

                    FEC = (TSS) -f (MLTSS/ATC RATIO)

                    i.e., FEC at 160 mg/1 at ESTABLISHED RATIO

                    FEC = 160/800 = 0.20$

                    CHECK CASE A

                    SLU IN = 14.0 x 0.032 = 0.448

                    SLU OUT = (4.0 x 0.10?) + (10.0 x 0.002)

                            = 0.428 + 0.020 = 0.448

                    CHECK CASE B

                    SLU IN = 14.0 x 0.032 = 0.448 MILLION SLU/DAY

                    SLU OUT = (4.0 x 0.112) + (10.0 x 0.0) = 0.448

NOTE: - AT CONSTANT CSP,  THE EFFLUENT SOLIDS LOSS WOULD REDUCE THE AMOUNT
        AND CONCENTRATION OF SLUDGE WITHDRAWN FOR RETURN.   THIS COULD ALSO
        DECREASE ATC IN THE NEXT PROCESS CYCLE.

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Environmental Prctaotlon Agency
Library, HegIon V
1 North 18 acker Drive
Chicago, Illinois  60606

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