Parameter & design criteria*

Equation* & obtained value

Sludge age, θc = 10 days

Half-saturation coefficient: Ks = 20 mg/l

maximum specific growth rate, m = 4.28 d−1

Endogenous respiration coefficient,

Kd = 0.1 d−1 at (15˚C)

EffluentCOD , S = K S ( 1 + K d SRT ) SRT ( m K d ) 1 = 1 m g COD / l

Design flow, Qave = 30,000 m3/day

biodegradable COD, bCOD = 1.6 × BOD = 340 mg/l

oxidizable ammonia concentration, NOx = 49.3 mg/l

yield coefficient, Y = 0.5

growth yield of nitrifying bacteria, yn = 0.12 decay constant of nitrifying bacteria,

Kdn (15˚C) = 0.065 d−1

fraction of biomass accumulated during decay, fd = 0.15

inert material in influent wastewater,

X o , i = 21.5 m g / l

solids production,

p x , b i o Q Y ( S o S ) 1 + ( k d ) SRT + Q y n N O x 1 + ( k d n ) SRT + f d k d Q Y ( S o S ) 1 + ( k d ) SRT SRT = 2443.5 kg / d

total solids, Px,T

P x , T = p x , b i o + Q X o , i = 3088.5 kg / d

MLVSS concentration =3500 mg/l

V = P x , T MLVSS = 8824 m 3

H.D.T = 2 h

V a n o x = H .D .T Q a v e / 24 = 2500 m 3

Effluent nitrate concentration, N O e = 25 mg / l

recycle nitrate = N O x N O e = 24.3 mg/ l

I R = N O x / N O r 1 = 1.03

based on Metcalf & Eddy SDNR = 0.35 g/g∙d (15˚) = 0.31

X a n o x = Q S R T V e r a Y ( S o S ) 1 + ( k d ) S R T I R I R + 1 = 1170 mg/l

F M a n o x = Q S o V a n o x X a n o x = 3.5 d 1

Noxfeed = Q I R N O r = 751 kg / d

NOrreduce = V a n o x SDNR X a n o x = 907 kg / d

Capacityratio = NOreduce Noxfeed = 1.2

Return sludge ratio Qr/Q = 0.8

concentration of recycle sludge, Xr = 10,000 mg/l

θ c = V X ( Q W X r ) + ( Q e X e )

sludgewasterate , Q W = 311 m 3 / d