activated sludge modeling

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    Modeling SuspendedModeling Suspended

    Growth SystemsGrowth Systems

    CE421/521CE421/521

    Environmental BiotechnologyEnvironmental Biotechnology

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      !eactor per"ormance

    as a "unction o" S!#$

      %ails to account "or&

    ' (articulate removal rate

    '  )naero*ic conditions

    ' +aria*le "low and

    loading

    ' Biological nutrient

    removal

    1)ˆ(

    )1(

    −−

    +=

    b

    bk S 

    c

    c s

     µ θ 

    θ 

    θ 

    θ 

    θ 

    c

    cb

    S S Y 

     X +

    =1

    )( 0

    Monod E,uation and -ni"ied ModelMonod E,uation and -ni"ied Model

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    .nternational )ssociation on ater.nternational )ssociation on ater

    0uality )ctivated Sludge Model 10uality )ctivated Sludge Model 1

    .)0)SM 13.)0)SM 13' .n 167 .)0 appointed a tas8 group to

    develop a model$

    ' .n 197 )SM 1 was completed$

    '  )SM 1 a*le to predict per"ormance o"solu*le and particulate su*strate removal7nitri"ication and denitri"ication under steadystate and dynamic conditions$

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     )SM 1 )SM 1

    ' #rac8s 16 individual components through

    eight separate processes$

    '  )ssumes heterotrophic growth under

    ano:ic conditions$

    ' ;imited anaero*ic activity$

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    .)0 )SM 2.)0 )SM 2

    ' .n 157 )SM 2 was released capa*le o"

    trac8ing *iological phosphorus "lows$

    '

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     )SM 2 )SM 2

    ' #rac8s 1 separate components through 1 processes$

    ' 22 stoichiometric coe""icients and 42 8inetic parameters

    '  )mmoni"ication and hydrolysis simpli"ied to stoichiometricterms= i$e$ rates implicit$

    ' .ncludes anaero*ic "ermentation7 upta8e o" acetate7"ormation o" (>B and (>)s7 and release o" solu*le

    phosphate "rom hydrolysis o" polyphosphate$

    ' Several assumptions made that constantly need revision as8nowledge evolves$

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     )ctivated Sludge Models )ctivated Sludge Models

    ' Cannot solve analytically$

    ' -se computer algorithm *ased on numerical

    techni,ues$

    ' B.?.

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    Steadystate per"ormance Steadystate per"ormance

    (articulate versus Solu*le(articulate versus Solu*le

    ' (articulate hydrolysis is a

    rate limiting step$

    '  ) particulate "eedre,uires a longer S!# to

    achieve treatment$

    ' (articulates compose allo" M;SS at low >!#s and

    active "raction is washed

    out$

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    Aynamic per"ormance (articulateAynamic per"ormance (articulate

    and Solu*leand Solu*le

    ' %low su*strate

    concentrations vary

    giving a diurnal

    pattern$

    ' (articulate and

    solu*le "eeds have

    di""erent e""ects on

    per"ormance$

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    Aenitri"icationAenitri"ication

    ' Aenitri"ication   ?rganics are electron

    donor 

     

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    Aenitri"icationAenitri"ication

    ' ?:ygen is pre"erred

    electron acceptor@

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    Aiurnal "low with di""erent aeration strategiesAiurnal "low with di""erent aeration strategies

    ' Single CS#! may *e

    set to&

      Maintain a constant

    dissolved o:ygenconcentration in the

    tan8

      Constant o:ygen "low

    into tan8

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    Modi"ied ;udac8 Ettinger Modi"ied ;udac8 Ettinger 

    ' -se an ano:ic *asinand an aero*ic *asinto select "ordenitri"ication a"ternitri"ication@

    ' hy denitri"yD

    ' here would youplace ano:ic selectorin "low schemeD

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    E""ect o" S!# on M;EE""ect o" S!# on M;E

    ' S!# is *iomass in

    system divided *y

    *iomass wasted "rom

    system where systemincludes *oth aero*ic

    and ano:ic *asins@

    CS#!

    M;E

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    M;EM;E

    ' !ecycle a""ectsper"ormance in M;E

    ' Greater recycle leadsto&