Activated Sludge Aeration Tank Calculations - S.I. Units
Workbook Contents
Click on tabs at the bottom of the screen to access the following:
(Parameter values entered here will be used in the other worksheets)
(tank volume based on volumetric loading, HRT, or F:M ratio)
(waste activated sludge and recycle activated sludge rates)
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Tab 1. Contents (current tab)
Tab 2. Input Wastewater Information
Tab 3. Aeration Tank Sizing Calculations
Tab 4. Aeration Tank Operations Calculations
Tab 5. Oxygen Requirement/Blower sizing Calculations
Activated Sludge Aeration Tank Calculations - S.I. Units
Workbook Contents
NOTE: The cells containing formulas are locked (protected) to avoid the possibility of inadvertently typing over any of the formulas. You may, however, adjust the number of decmal places for any of the cells.
(Parameter values entered here will be used in the other worksheets)
(tank volume based on volumetric loading, HRT, or F:M ratio)
(waste activated sludge and recycle activated sludge rates)
NOTE: The cells containing formulas are locked (protected) to avoid the possibility of inadvertently typing over any of the formulas. You may, however, adjust the number of decmal places for any of the cells.
Activated Sludge Waste Water Treatment Calculations - U.S. units
Input of Values for Wastewater Parameters
Enter values in yellow cells only.
INPU
T IN
FOR
MA
TIO
N
Note that these parameter values will be used in the other worksheets.
Input Information
5678.1
160
2100
70%
Waste/recycle activated
6800
20
Copyright © McGraw-Hill Global Education Holdings, LLC. All rights reserved.
Design Wastewater Flow Rate, Qo = m3/d
Primary Effluent BOD5, So = g/m3
Aeration Tank MLSS, X = g/m3
% volatile MLSS, % Vol =
Sludge SS conc., Xw = g/m3
Secondary Effluent TSS, Xe = g/m3
Activated Sludge Waste Water Treatment Calculations - U.S. units
Input of Values for Wastewater Parameters
Note that these parameter values will be used in the other worksheets.
Activated Sludge Waste Water Treatment Calculations - S.I. unitsAeration Tank Sizing Calculations
INPU
T IN
FO
Parameter Values Transferred from Worksheet 2:
5678.1
160
2100
70%
Enter values in yellow cells only.
CA
LCU
LATI
ON
S/ R
ESU
LTS
1. Sizing Based on Volumetric Loading 0.5606
Design Aeration Tank Volume Values of other Design Parameters
Aer Tank Hydr. Retention Time: 6.851,621
Aer Tank F:M Ratio: 0.381
2. Sizing Based on Hydr. Retention Time 7.0
Design Aeration Tank Volume Values of other Design Parameters
1,656 Aer Tank Volumetric Loading: 0.549
Aer Tank F:M Ratio: 0.373
3. Sizing Based on F:M Ratio 0.35
Design Wastewater Flow Rate, Qo = m3/d
Primary Effluent BOD5, So = g/m3
Aeration Tank MLSS, X = g/m3
% volatile MLSS, % Vol =
Design Vol. Loading, VL =
Aeration Tank Volume, V = m3
Design Aeration Tank HRT =
Aeration Tank Volume, V = m3
Design F:M Ratio, F:M =
CA
LCU
LATI
ON
S/ R
ESU
LTS
Design Aeration Tank Volume Values of other Design Parameters
Aer Tank Volumetric Loading: 0.5151,766
Aer Tank Hydr. Retention Time: 7.46
Copyright © McGraw-Hill Global Education Holdings, LLC. All rights reserved.
Aeration Tank Volume, V = m3
Activated Sludge Waste Water Treatment Calculations - S.I. units References and Equations
Aeration Tank Sizing Calculations A flow diagram of the activated sludge process is shown below along with the equations used in this worksheet. For more details and background information on the activated sludge process and its design and operation calculations, see the following references:
The symbols used in the flow diagram at the left andthe equations below are as follows:
Enter values in yellow cells only.
Values of other Design Parameters
hr
waste activated sludge and recycle activated sludge
are taken to be equal to that in the effluent stream.
hr
Equations Used for These Calculations:
Values of other Design Parameters
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7 Suspended Growth Design Practice
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1 Activated Sludge
Handbook of Environmental Engineering Calculations, 2nd Ed, Sec 1.7.21 Activated Sludge Process
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Sec. 14.1.3 Activated Sludge Environment
Q is volumetric flow rate in m3day
S is BOD5 concentration in g/m3
kg BOD5/day/m3 X is total suspended solids concentration in g/m3
The subscript o refers to the primary effluent stream.
The subscript e refers to the secondary effluent stream.
The subscript w refers to the waste act. sludge stream.
The subscript r refers to the recycle act. Sludge stream. kg BOD5/day/kg MLVSS NOTE: Based on an assumption of no biological
degradation in the secondary clarifier, the BOD5 in the V is the volume of the aeration tank in m3.X is the mixed liquor suspended solids concentration
in the aeration tank in g/m3.
Volumetric Loading: VL = [(So*Qo)/V]/(1000 g/kg)
kg BOD5/day/m3 hydraulic Loading: HRT = 24*V/Qo
kg BOD5/day/kg MLVSS F:M Ratio: F:M = (So*Qo)/(%Vol*X*V)
NOTE: The conversion factors in these equations are: 1000 g/kg and 24 hr/day
kg BOD5/day/kg MLVSS
Values of other Design Parameters
hr
The sources for the information in the above table are 1) Hydraulic Retention Time values:
and 2) Volumetric Loading and F:M Ratio values:
lb BOD5/day/1000 ft3
Standard Handbook of Environmental Engineering, 2nd Ed, Table 6-43 and Table 6-44
Operation of Municipal Wastewater Treatment Plants, MOP No. 11, 6th Ed., Table 20.1
A flow diagram of the activated sludge process is shown below along with the equations used in this worksheet. For more details and background information on the activated sludge process and its
The symbols used in the flow diagram at the left andthe equations below are as follows:
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7 Suspended Growth Design Practice
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1 Activated Sludge
Handbook of Environmental Engineering Calculations, 2nd Ed, Sec 1.7.21 Activated Sludge Process
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Sec. 14.1.3 Activated Sludge Environment
is volumetric flow rate in m3day
concentration in g/m3
is total suspended solids concentration in g/m3
The subscript o refers to the primary effluent stream.
The subscript e refers to the secondary effluent stream.
The subscript w refers to the waste act. sludge stream.
The subscript r refers to the recycle act. Sludge stream.
is the volume of the aeration tank in m3. is the mixed liquor suspended solids concentration
in the aeration tank in g/m3.
: The conversion factors in these equations are: 1000 g/kg and 24 hr/day
The sources for the information in the above table are 1) Hydraulic Retention Time values:
Standard Handbook of Environmental Engineering, 2nd Ed, Table 6-43 and Table 6-44
Operation of Municipal Wastewater Treatment Plants, MOP No. 11, 6th Ed., Table 20.1
Activated Sludge Waste Water Treatment Calculations - S.I. units
Aeration Tank Operation Calculations
Enter values in yellow cells only.
INPU
T IN
FOR
MA
TIO
N
Input Information
1,699
12
Parameter Values Transferred from Worksheet 2:
5678.1
160
2100
70%
20
6800
RES
ULT
S
Activated Sludge Operational Parameters
2,537
27.0
0.364 kg BOD/day/kg MLVSS
Aeration Tank Volume, V =
Target Sludge Retention Time, SRT =
Design Wastewater Flow Rate, Qo =
Primary Effluent BOD, So =
Aeration Tank MLSS, X =
% volatile MLSS, % Vol =
Secondary Effluent TSS, Xe =
Waste/Recycle Act. Sludge Conc., Xw =
Recycle Act. Sludge Rate, Qr = m3/d
Waste Act. Sludge Rate, Qw = m3/d
Aer. Tank F:M Ratio, F:M =
RES
ULT
S
activated sludge are sent back into the wastewater stream.
Copyright © McGraw-Hill Global Education Holdings, LLC. All rights reserved.
NOTE: In Calculating Qw, the effluent flow rate, Qe is taken to be equal to the influent flow
rate, Qo, based on the assumption that liquid streams separated from the waste
Activated Sludge Waste Water Treatment Calculations - S.I. units References and Equations
Aeration Tank Operation Calculations A flow diagram of the activated sludge process is shown below along with the equations used in this
worksheet. For more details and background information on the activated sludge process and its design and operation calculations, see the following references:
days
Parameter Values Transferred from Worksheet 2:
degradation in the secondary clarifier, the soluble
is taken to be equal to that in the effluent stream.
kg BOD/day/kg MLVSS
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7 Suspended Growth Design Practice
m3 Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1 Activated Sludge
Handbook of Environmental Engineering Calculations, 2nd Ed, Sec 1.7.21 Activated Sludge Process
Operation of Municipal Wastewater Treatment Plants, MOP No. 11, 6th Ed., Sec. 20.1 Activated Sludge
m3/d
g/m3
g/m3
g/m3
g/m3
NOTE: Based on an assumption of no biological
BOD5 in the waste and recycle activated sludge
Recycle Activated Sludge Rate: Qr = QoX /(Xw - X)
Waste Activated Sludge Rate: Qw = (V*X/SRT - Qe*Xe)/Xw
activated sludge are sent back into the wastewater stream.
Copyright © McGraw-Hill Global Education Holdings, LLC. All rights reserved.
The source for the information in the above table is:
and
is taken to be equal to the influent flow F:M Ratio: F:M = (So*Qo)/(%Vol*X*V) , based on the assumption that liquid streams separated from the waste
Standard Handbook of Environmental Engineering, 2nd Ed, Table 6-43 and Table 6-44
Operation of Municipal Wastewater Treatment Plants, MOP No. 11, 6th Ed., Table 20.1
References and Equations
A flow diagram of the activated sludge process is shown below along with the equations used in this
worksheet. For more details and background information on the activated sludge process and its design and operation calculations, see the following references:
The symbols used in the flow diagram at the left andthe equations below are as follows:
degradation in the secondary clarifier, the soluble
is taken to be equal to that in the effluent stream.
Equations Used for These Calculations
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7 Suspended Growth Design Practice
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1 Activated Sludge
Handbook of Environmental Engineering Calculations, 2nd Ed, Sec 1.7.21 Activated Sludge Process
Operation of Municipal Wastewater Treatment Plants, MOP No. 11, 6th Ed., Sec. 20.1 Activated Sludge
Q is volumetric flow rate in m3dayS is BOD5 concentration in g/m3
X is total suspended solids concentration in g/m3
The subscript o refers to the primary effluent stream.The subscript e refers to the secondary effluent stream.
The subscript w refers to the waste act. sludge stream.The subscript r refers to the recycle act. Sludge stream.
: Based on an assumption of no biological V is the volume of the aeration tank in m3.
X is the mixed liquor suspended solids concentration
in the waste and recycle activated sludge in the aeration tank in g/m3.
Recycle Activated Sludge Rate: Qr = QoX /(Xw - X)
Waste Activated Sludge Rate: Qw = (V*X/SRT - Qe*Xe)/Xw
The source for the information in the above table is:
F:M Ratio: F:M = (So*Qo)/(%Vol*X*V)
Standard Handbook of Environmental Engineering, 2nd Ed, Table 6-43 and Table 6-44
Operation of Municipal Wastewater Treatment Plants, MOP No. 11, 6th Ed., Table 20.1
Activated Sludge Waste Water Treatment Calculations - S.I. units
Oxygen Requirements/Blower Sizing Calculations
and average ww flow rates be identified and that the oxygen requirement rates be calculated for each.
INPU
T IN
FOR
MA
TIO
N
5678.1 (Value transferred from Worksheet 2)
160 (Value transferred from Worksheet 2)
20
20
80%
12.0 days
0.6
0.06 kg VSS/d/kg VSS
20.0% (from diffuser mfr or vendor)
0.02989 bar (from diffuser mfr or vendor)
3.6576 m (from installation or plans)
10
NOTE: To aid in setting the design WW flow rate for these calculations, it is recommended that the maximum, minimum
User Input Information - See Tables below right for typical values of kd and Y and of oxygen transfer parameters
Design WW Flow Rate, Qo = m3/d
Primary Effluent BOD, So = g/m3
Permitted Sec Effl BOD, BODe = g/m3
Permitted Sec Effl TSS, TSSe = g/m3
% volatile solids in Effl TSS , %Vol =
Sludge Retention Time, SRT =
Synthesis Yield Coefficient, Y = kg VSS/kg BOD5
Endog. Decay Coeff (at 20oC), kd20 =
Std. O2 transfer Efficiency, SOTE =
Press. drop across diffuser, DPdiff =
Depth of Diffuser, ddiff =
Design ambient air Temperature, Ta = oC
1.014 bar
CO
NST
AN
TS/C
ON
V. F
AC
TOR
S
Constants and Conversion Factors used in the Calculations
1.024
8.3145 kN-m/kgmole-K
9.807
Conversion Factor: 1000 g/kg
Conversion Factor: 60 min/hr or sec/min
1.42 kg COD/kg VSS
4.57
A. Oxygen Requirement/Blower Specifications (BOD Removal Only)
RES
ULT
S
Air Requirement/Blower Design Calculations/Results
4.778
0.047 kg VSS/d/kg VSS
Standard Pressure and Temperature for Sm3/m calculation (per ASME & CAGI) - Changeable by User
Standard Pressure, PS =
Temp. coeff for kd, q, =
Ideal Gas Law Constant, R =
Specific Weight of water, gH2O = kN/m3
cbCOD (BODult) equivalent of VSS:
O2 equivalent of NH3-N: kg O2/kg NH3-N
Effluent Soluble BOD, Se = g/m3
Endog. Decay Coeff (at 20oC), kd20 =
RES
ULT
S0.383
34.86 kg/hr
14.0%
B. Oxygen Requirement/Blower Specifications (BOD Removal and Nitrification)
RES
ULT
S
Air Requirement/Blower Design Calculations/Results
72.16 kg/hr
14.0%
submergence depth. Oxygen depletion due to transfer from rising bubbles is not considered, thus the AOTE is then slightly
overstated. Hence the the air delivery requirement is then slightly underestimated.
Copyright © McGraw-Hill Global Education Holdings, LLC. All rights reserved.
Observed Yield (with recycle), Yobs = kg VSS/kg BOD5
Required O2 flow rate =
Act. O2 transfer Efficiency, AOTE* =
O2 required per day =
Act. O2 transfer Efficiency, AOTE* =
* NOTE: The calculation of actual oxygen transfer efficiency (AOTE) considers the mean bubble position to be half the diffuser
Activated Sludge Waste Water Treatment Calculations - S.I. units
Oxygen Requirements/Blower Sizing Calculations A flow diagram of the activated sludge process is shown below along with the equations used in this worksheet. For more details and background information on the activated sludge process and its design and operation calculations, see the following references:
and average ww flow rates be identified and that the oxygen requirement rates be calculated for each.
Enter values in yellow cells only
35
0.50
1.014 bar (ambient pressure at site)
Design wastewater Temperature = 10
0.67
70%
Ratio of oxygen transfer rate in wastewater
0.9
Ratio of D.O. saturation in wastewater to that
1.0
D.O saturation conc. for clean water at
11.28 waste activated sludge and recycle activated sludge
D.O conc. to be maintained are taken to be equal to that in the effluent stream.
2.0
0.8
0.021 bar (due to filter, silencer, etc.)
: To aid in setting the design WW flow rate for these calculations, it is recommended that the maximum, minimum
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7, Suspended Growth Design Practice
User Input Information - See Tables below right for typical values of kd and Y and of oxygen transfer parameters Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1. Activated Sludge
Influent TKN, TKNo = g/m3 Handbook of Environmental Engineering Calculations, 2nd Ed, Sec 1.7.21. Activated Sludge Process
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Sec. 14.1.3. Activated Sludge Environment
Effluent NH4-N Concentration, Ne = g/m3
Design Barometric Press., Patm =
oC
Ratio of BOD5/BODu, f =
Blower efficiency, h =
to that in clean water, a =
in clean water at same T & P, B = NOTE: Based on an assumption of not biological
degradation in the secondary clarifier, the BOD5 in the
wastewater temp. & 1 atm, Cs = g/m3
for WW trtmt operation, CL = g/m3
Diffuser fouling factor, F =
Pressure drop at blower inlet, DPin = Temperature correction for kd: kd at temp. T = (kd at 20oC)q(T - 20) ( T is in oC )
20
Constants and Conversion Factors used in the Calculations
Saturation D.O. in water
9.17 These two oxygen requirement equations are based on:
Molecular weight of air = 28.97
Molecular weight of oxygen = 32
1.014 bar The equation for AOTE is based on information in:
Oxygen mole fraction in air = 0.209
Conversion Factor: 24 hr/day
Conversion Factor: 100 kPa/bar
subscript s is for standard conditions.)
A. Oxygen Requirement/Blower Specifications (BOD Removal Only)
Air Requirement/Blower Design Calculations/Results
1.193 bar
1.205
Observed Yield (with recycle): Yobs = Y/(1 + kd*SRT)Standard Pressure and Temperature for Sm3/m calculation (per ASME & CAGI) - Changeable by User
Required O2 Flow Rate (BOD removal only): kg/day O2 = Qo*(So - Se)*[(1/f) - 1.42 Yobs]/1000 Standard Temperature, TS = oC
Required O2 Flow Rate (BOD removal & Nitrification):
NOTE: With nitrification, Se is typically taken to be zero because of the long SRT used.
at 20oC & 1 atm, Css = g/m3
Nalco Water Handbook, 3rd Ed., Equations 23.6 and 23.7
Actual O2 transfer effic. = AOTE = SOTE*a*F*[(B*(PD/Pstd)*Cs -CL)/Css]1.024(T-20)
Atmospheric Press. at sea level, Pstd =
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1. Activated Sludge
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Equation 14.34
and: Metcalf & Eddy, Wastewater Engineering, Treatment and Disposal, 4th Ed, Equation 5-55, McGraw-Hill, 2003.
Des. Std Flow Rate: SCMM = (kg/hr O2/AOTE)*MWair/[O2 fract in air)(MWO2)(rair)(60 min/hr)]
Des. Actual Air Flow Rate: ACMM = SCMM(TAa/TAs)(Ps/Pa)
( TA is abs temp., P is abs press., subscript a is for actual conditions and
Blower outlet pressure: PB2 = Patm + DPdiff + [gH2O*ddiff/(100 kPa/bar)]
Pressure at Mid Depth, PD =
Standard Air Density, rair = kg/m3
(from Ideal Gas Law)
15.0
10.45 The source of values in the above table is:
(at delivery point)
1.402 bar
B. Oxygen Requirement/Blower Specifications (BOD Removal and Nitrification)
Air Requirement/Blower Design Calculations/Results
30.96
21.63 (at delivery point) The sources for the information in the above table are:
1.402 bar
Company, 2003.
submergence depth. Oxygen depletion due to transfer from rising bubbles is not considered, thus the AOTE is then slightly For an example calculation of oxygen and air requirement, see:
overstated. Hence the the air delivery requirement is then slightly underestimated.
Copyright © McGraw-Hill Global Education Holdings, LLC. All rights reserved.
Design Air Flow Rate, SCMM = mstd3/min
Design Air Flow Rate, ACMM m3/min
Handbook of Environmental Engineering Calculations, 2nd Ed., Table 7.12
Blower outlet pressure, PB2 =
Design Air Flow Rate, SCMM = mstd3/min
Design Air Flow Rate, ACMM m3/min
Blower outlet pressure, PB2 = Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1. Activated Sludge and: Metcalf & Eddy, Wastewater Engineering, Treatment and Disposal, 4th Ed, Equation 5-55, McGraw-Hill Book
The calculation of actual oxygen transfer efficiency (AOTE) considers the mean bubble position to be half the diffuser
Handbook of Environmental Engineering Calculations, 2nd Ed., Example 1.A, steps 13 - 16
References and Equations
A flow diagram of the activated sludge process is shown below along with the equations used in this worksheet. For more details and background information on the activated sludge process and its design and operation calculations, see the following references:
The symbols used in the flow diagram at the left, in
the equations below, and in the worksheet calculations
are as follows:
waste activated sludge and recycle activated sludge
are taken to be equal to that in the effluent stream.
Equations Used for These Calculations See descriptions of the parameters above and in the User Entry section to the left.
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7, Suspended Growth Design Practice
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1. Activated Sludge
Handbook of Environmental Engineering Calculations, 2nd Ed, Sec 1.7.21. Activated Sludge Process
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Sec. 14.1.3. Activated Sludge Environment
Q is volumetric flow rate in m3day
S is BOD5 concentration in g/m3
X is total suspended solids concentration in g/m3
The subscript o refers to the primary effluent stream.
The subscript e refers to the secondary effluent stream.
The subscript w refers to the waste act. sludge stream.
The subscript r refers to the recycle act. Sludge stream.
NOTE: Based on an assumption of not biological
degradation in the secondary clarifier, the BOD5 in the V is the volume of the aeration tank in m3.
X is the mixed liquor suspended solids concentration
in the aeration tank in g/m3.
Temperature correction for kd: kd at temp. T = (kd at 20oC)q(T - 20) ( T is in oC )
These two oxygen requirement equations are based on:
See descriptions of the parameters in the User Entry section to the left.
The equation for AOTE is based on information in:
subscript s is for standard conditions.)
Observed Yield (with recycle): Yobs = Y/(1 + kd*SRT)
Required O2 Flow Rate (BOD removal only): kg/day O2 = Qo*(So - Se)*[(1/f) - 1.42 Yobs]/1000
Se = effluent soluble BOD = BODe - (f*1.42*% Vol*TSSe)
Required O2 Flow Rate (BOD removal & Nitrification):
kg/day O2 = Qo*{(So - Se)[1/f - 1.42 Yobs] + 4.57(TKNo - Ne)}/1000
NOTE: With nitrification, Se is typically taken to be zero because of the long SRT used.
Nalco Water Handbook, 3rd Ed., Equations 23.6 and 23.7
Actual O2 transfer effic. = AOTE = SOTE*a*F*[(B*(PD/Pstd)*Cs -CL)/Css]1.024(T-20)
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1. Activated Sludge
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Equation 14.34
and: Metcalf & Eddy, Wastewater Engineering, Treatment and Disposal, 4th Ed, Equation 5-55, McGraw-Hill, 2003.
Des. Std Flow Rate: SCMM = (kg/hr O2/AOTE)*MWair/[O2 fract in air)(MWO2)(rair)(60 min/hr)]
Des. Actual Air Flow Rate: ACMM = SCMM(TAa/TAs)(Ps/Pa)
TA is abs temp., P is abs press., subscript a is for actual conditions and
Blower outlet pressure: PB2 = Patm + DPdiff + [gH2O*ddiff/(100 kPa/bar)]
The source of values in the above table is:
The sources for the information in the above table are:
Company, 2003.
For an example calculation of oxygen and air requirement, see:
Handbook of Environmental Engineering Calculations, 2nd Ed., Table 7.12
Standard Handbook of Environmental Engineering, 2nd Ed, Sec 6.5.1. Activated Sludgeand: Metcalf & Eddy, Wastewater Engineering, Treatment and Disposal, 4th Ed, Equation 5-55, McGraw-Hill Book
Handbook of Environmental Engineering Calculations, 2nd Ed., Example 1.A, steps 13 - 16
The symbols used in the flow diagram at the left, in
the equations below, and in the worksheet calculations
Water and Wastewater Engineering Design Principles and Practice, Sec 23.7, Suspended Growth Design Practice
Design of Municipal Wastewater Treatment Plants, WEF MOP No. 8, 5th Ed., Sec. 14.1.3. Activated Sludge Environment
refers to the primary effluent stream.
refers to the secondary effluent stream.
refers to the waste act. sludge stream.
refers to the recycle act. Sludge stream.
is the mixed liquor suspended solids concentration