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活性污泥法设计

来源:九壹网
Activated Sludge Process Design Example(with nitrification)

1.Design InformationFlow rate Q =Influent BOD5 S0=Influent VSS X0=Effluent BOD5 Se=Effluent SS =Effluent VSS Xe =Effluent BOD5 S =Influent NH3-N SNH1 =Effluent NH3-N SNH =Growth yield YH =

YA =

Decay rate kd =

0.50.220.06

day-1

8,000

o

20,000m3/d (average day)200mg/L (soluble)02020137.4

mg/Lmg/Lmg/Lmg/Lmg/L (soluble)400

mg/Lmg/L

MLVSS/MLSS =0.8

Wasted sludge concentration XW =Plant altitude =

100

m25

Design temperature T =

mg/L

C

1-1.Nitrification EvaluationSelectm^A =0.75day-1

C =

KOA =bA =qX =

qmX = 1/(m^'A - bA) =fSA = qX / qmX =2.Aeration BasinSelect MCRT qX =Select MLVSS X =5.02.00.50.1010mg/Lmg/Lday-1days0.602.0

Thus nitrification happens

day-1

m^'A = m^AC/(KOA + C) =

102,000daysmg/L0.313

MLSS =2,500mg/L

Observed yield Yobs = Y/(1 + kdqX) =

Increase in VSS PXH = YobsQ(S0 - S) =1,203kg/dReguired basin volume V = PXHqX/X =6,017m3Select basin depth D =5.0

mReguired basin area A = V/D =1,203m3Select basin length L =40mReguired basin width W = A/L =30

m3

SelectYA =0.22Neglect N comsumed for cell synthesisPXA = YA Q NOX / (1 + bAqX) =88kg/dPXT = PXH + PXA =

1,291

kg/d

Increase in MLSS PXMT =1,614

kg/d

Mass balance of wasted sludgePXMT = (Q - QW)SS + QWXWQW = (PXMT - Q SS)/(XW - SS) =152m3/d

Solids in wasted sludge =1,217kg/dSolids lost in effluent =

397kg/d

3.Oxygen and Air RequirementInfluent BODU SS1=294mg/LEffluent BODU SS =11mg/L

ThOR = Q(SS1 - SS) + 4.57 Q(SNH1-SNH) - 1.42 PXT =

Select

Csw =9.08mg/LC'sw =8.24mg/LC =2.0mg/L

a =

0.8

b =0.9

Fa = 1 - altitude/9450 =0.99

SOR = ThOR / [((C'swbFa – C)/Csw) (1.024)T-20 a] =

Air density r = PM/RT =1.184kg/m3

Select OTE =25%

SAR = [SOR/(r 0.232)]/OTE =

205,838m3/d =

Select SF =1.5AR = SAR x SF =

214

m3/min

4.Circular Secondary ClarifierSelect overflow rate =

22

m3

/m2

-dNecessary area for sedimentation =

909

m

2

7,485

kg/d

kg/d

143

m3/min

14,138Select clarifier diameter =Area of one clarifier =Min. clarifier number =Total clarifier area =Actual overflow rate =Select clarifier depth =Select RAS ration =Check HRT =

3.5

Check solid loading rate =5.Alkalinity RequirementSALK = 7.07(SNH1 - SNH) =Alkalinity demand =

203143942214.00.3hour2.9

2835,656

mm2

(provide additionl 1 clarifier for standby)m3/m2-dm

kg/m2-h

mg/L as CaCO3kg/d as CaCO3

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