Nitr if Ication

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    7 Dissolved OxygenIntroduction

    Oxygen Saturation

    Biochemical Oxygen Demand

    ReaerationStreeter-Phelps Equation

    Nitrification

    Sediment Oxygen Demand

    Photosynthesis and Respiration

    Expanded Streeter-Phelps EquationArtificial Re-aeration

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    Dissolved Oxygen

    Important for aquatic health DO standards typically 5 to 6 mg/L

    Redox chemistry

    Affects release of chemicals bound tosediments

    Anaerobic conditions => H2S

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    Oxygen Saturation

    ]})15.273/(101407.2

    )15.273/(754.10107674.1[)15.273/(10621949.8

    )15.273/(10243800.1)15.273/(10642308.6

    )15.273/(10575701.1103934411.1exp{),(

    23

    2411

    31027

    52

    ++

    ++

    +++

    ++=

    Tx

    TxSTx

    TxTx

    TxxSTcs

    =

    )1)(1(

    )1)(/1(),(),,(

    wv

    wv

    ssp

    pppSTcpSTc

    ])15.273/(1016961.2)15.273/(108407.38575.11exp[ 253 ++= TxTxpwv

    285 10436.610426.1000975.0 TxTx +=

    Standard Methods (1995)

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    Cs (T, S, p)T=0o 10 20 30

    Effect of p (S=0)

    p = 1 atm (z=0) 14.6 11.3 9.1 7.6

    p = 0.89 (1000m) 12.9 19.9 8.0 6.7p = 0.79 (2000m) 11.4 8.8 7.1 5.9

    Effect of S (p=0)

    S = 0 PSU 14.6 11.3 9.1 7.7

    S = 10 13.6 10.6 8.6 7.2

    S = 35 11.4 9.0 7.4 6.2

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    Processes affecting DO

    BOD (-)

    Re-aeration (+/-)

    P(+)/R(-)

    Inflow

    (+/-)

    SOD (-)

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    Biochemical Oxygen DemandOrganic wastes are food formicroorganisms Oxygen consumed in process

    Self-purification (bio-degradation) innatural waters

    Biological stage of WWT

    Other chemicals exert oxygen demand C2H6O2

    NaHSO3

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    Theoretical Oxygen Demand

    43

    3222 )2

    3

    2

    3

    2()

    4

    5

    4

    3

    24(

    POdH

    cNHOHdca

    nCOOdcba

    nPNOHC dcban

    +

    ++=+++

    OHHNOONH 22232

    3++=+ +

    =+322 2

    1NOONO

    Carbonaceous BOD (CBOD)

    Nitrogenous BOD (NBOD)

    Issues

    Different types of wastes Some not labile

    Rates vary (nitrification)

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    Practical Measures of Oxygen Demand

    BOD Traditional water quality measure

    Cumbersome and time-consuming

    COD

    Easy to measure

    TOC State variable in WQ models

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    Traditional BOD

    Practical measure of O2debt How much DO would decrease due to

    respiration of organic wastes

    BOD Jar Test Observe the decline of DO over time (e.g.

    5 days) Extrapolate to ultimate demand

    Used for wastewater and natural waters

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    BOD Jar TestPrecautions

    No photosynthesis

    Enough initial O2

    Adequate dilution (WW) Enough microorganisms

    Non toxic sample

    Only carbonaceous BOD

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    [DO]

    time

    y5 = BOD5

    yu =

    BODu

    y(t)

    0

    0 5 days

    )1(1tK

    eLy

    =15

    5

    1K

    e

    LL

    =

    2011 )20(

    =TKK

    047.1~;5.01.0~)20( 11 dK

    In rivers

    sdr KKK +=

    hwK ss /=

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    Other Measures of BOD

    COD Easy to measure

    Much quicker

    TOC State variable in WQ models

    Relationship to BOD (Metcalf & Eddy) BOD5/COD ~ 0.4 to 0.8

    BOD5/TOC ~1.0 to 1.6

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    Stream ReaerationWater side control

    Flux F ~ DO deficit

    Piston velocity [LT-1]

    kL ~ kw

    Reaeration rate [T-1]

    Ka

    = K2

    = kw

    /h

    Theories

    Stagnant Film

    Surface Renewal

    H

    c

    cszw

    h F=kL(cs-c)

    = zw

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    Stream ReaerationStagnant Film

    kL = D/zw

    Surface Renewal

    zw ~ (Dt)0.5 t ~ h2/Ez ~ h/u

    zw ~ (Dh/u)0.5

    kL ~ (Du/h)0.5

    Ka ~ (Du/h3)0.5

    H

    c

    F=kL(cs-c)

    cszw

    h

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    Stream Reaeration Formulae

    u in m/s, h in m, T=20o

    5.1

    5.093.3h

    uKa = OConnor-Dobbins

    (1958)

    Churchill et

    al. (1962

    Owens &Gibbs

    (1964)

    67.1

    0.5

    h

    uKa =

    85.1

    67.03.5

    h

    uKa =

    Kovar, 19760.1

    0.3

    0.4

    0.50.60.8

    1

    2Depth

    (ft.)

    3

    456

    8

    10

    20

    30

    40O'Connor

    Owens

    .05

    0.5

    5

    10

    105

    Churchill

    50100

    1

    50

    0.2Velocity (ft./sec.)

    0.3 0.4 0.6 0.8 1 2 3 4 5 6

    0.1

    Figure by MIT OCW.

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    Other formulationsRate of Energy Dissipation (Tsivoglou

    & Wallace, 1972)

    Melching and Flores (1999)

    uSuL

    LSTH ==

    /

    Pool and Riffle Reaeration Coefficient

    Ka

    CV

    Q < 0.56 517(uS)0.524Q-0.242 0.61

    Q > 0.56 596(uS)0.528Q-0.136 0.44

    Channel Control

    Q < 0.56 88(uS)0.313H-0.353 0.59

    Q > 0.56 142(uS)0.333H-0.66W-

    0.243

    0.60

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    1-D Analysis

    (Streeter-Phelps, 1925)

    Continuity

    lqAu

    xt

    A=

    +

    )(

    Mass Transport

    )()()()(eiL rrA

    x

    cAE

    xAuc

    xAc

    t++

    =

    +

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    BOD (c = L)

    LKr ri =ALqre /ll=

    =x

    xu

    dx

    0)(

    A

    LLqLK

    dx

    dLu r

    )( += ll

    )( LLLKd

    dLr

    +=l

    [ ] { }])(exp[1)(

    )(exp)(

    +

    +++= r

    r

    ro KK

    LKLL l

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    DO (c = c)LKr di =

    )(/ ccKAcqr sae += ll

    A

    ccqccKLK

    dx

    dcu sad

    )()(

    ++= ll

    )()( ccccKLKd

    dcsar ++= l

    ccs =

    ]})(exp[])({exp[

    )()(

    ]})(exp[1{))((

    ])(exp[)(

    ++

    +

    +

    +++

    ++=

    ar

    r

    o

    ra

    d

    a

    ar

    d

    ao

    KvK

    K

    LL

    KK

    K

    vKvKvK

    LKK

    l

    l

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    Streeter-Phelps-additional comments

    cmin

    and xmin

    can be calculatedanalytically

    Multiple sources handled by

    superposition or re-initialization atstream confluences

    Procedures for anoxic conditions

    Neglect of longitudinal dispersion?

    Additional terms

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    Nitrification

    (2)(32/14) = 4.5743

    3222 )

    2

    3

    2

    3

    2

    ()

    4

    5

    4

    3

    24

    (

    POdH

    cNHOHdca

    nCOOdcba

    nPNOHC dcban

    +

    ++=+++

    OHHNOONH 22232

    3++=+ +

    =+ 3222

    1NOONO (0.5)(32/14) = 1.14

    Theoretical (upper bound) NBOD

    NNONNHNOrgNBOD ++= 23 14.1)(57.4

    TKN = total Kjeldalh nitrogenTKNNBOD 57.4

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    [DO]

    CBOD

    NBOD

    0

    time0

    Time scale for NBOD ~ 10 days => often insignificant in rivers

    If important, separate CBOD & NBOD analyses required

    May be better to include nitrogen species as state variables

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    Sediment Oxygen Demand (SOD)

    BOD in sediments

    Significant downstream from outfalls orfollowing algal blooms

    SB = 0.1 to 1 g/m2-d

    re = SB/h

    Oth order process

    0.1 to 1 mg/L-d (h = 1 m)

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    SOD (contd)Measured

    in situwith benthic flux chambers

    in lab with core

    Calculated from organic carbon contentof settled solids

    Calibrated from oxygen modelComplication: extraneous sources

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    Benthic Flux Chambers

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    Zebra Mussels

    Algal Photosynthesis and

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    Algal Photosynthesis and

    Respiration

    Photosynthesis (primary production) =>fixation of CO2 by autotrophic bacteria

    Reverse is respiration

    6CO2 + 6H2O C6H12O6 + 6O2

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    P/R (contd)Limitations on primary production:

    Light

    Temperature

    Nutrients

    Time and space dependent

    Diurnal variation Depth variation

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    P(t)

    Pm

    Pa

    24 hf0 t

    ma Pf

    P24

    2= f = photoperiod (hrs)

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    EPA (1985)

    Curve A

    Curve B

    Wyman Creek, Calif

    August 6, 1962

    Average 10.1 MG/L

    River Ivel, England

    May 31, 1959

    Average 10.4 MG/L

    7

    8

    9

    10

    11

    12

    13

    0600 06000900 1200N 1500 1800 2100 2400 0300

    Hours

    DissolvedO

    xygenMG/L

    Figure by MIT OCW.

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    Estimation of P/RIn situ measurements w/ Light & DarkBottles

    LKt

    cc

    R ddark

    to

    = mg/L-d; L = ultimate

    BOD of filtered sample

    dark

    ot

    light

    ot

    t

    cc

    t

    cc

    tP

    =)(

    P(t) is averaged over time t. t = 24 hrs => Pa;

    t< 24 h => fit to diurnal variation using f

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    Pm

    t24 hf

    Pa

    0

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    Estimation of P/R (contd)

    Calibrate to observed diurnal variationin P(t) using estimated Ka

    Delta Method (Chapra and DiToro, 1979)

    Correlate with chlorophyll-a

    aChlP = 25.0

    aChlR = 025.0

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    Expanded Streeter-Phelps Eqs*

    h

    RP

    h

    S

    ccccKLKLKd

    dc

    u

    B

    saNNr

    )(

    )()(

    +++=

    l

    CBOD NBOD* Reaeration Lat Inflow SOD P/R

    [ ] { }])(exp[1)()(exp)(

    +

    +++=

    rr

    ro KK

    L

    KLL

    l

    ])(exp[)( vKLL NNoN +=

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    Expanded S-P (contd)

    { }

    { }

    { }

    { })])(exp[1)(

    )/(

    ])(exp[])(exp[)(

    ])(exp[1))((

    ])(exp[])(exp[)(

    ])(exp[

    ++

    ++

    +

    ++++

    ++

    +

    ++=

    a

    a

    B

    aN

    Na

    NoN

    a

    ar

    d

    ar

    r

    o

    ra

    d

    ao

    KK

    HSRP

    KKKK

    LK

    KKK

    LK

    KKK

    LL

    KK

    K

    K

    l

    l

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    Expanded S-P (contd)Lateral BOD sources w/o significant inflow

    ALqLrd

    ll= 0= ux/=

    [ ]

    { }

    [ ] [ ]

    [ ])/exp(1

    )/exp()/exp()(

    )/exp(1

    )/exp()/exp()(

    )/exp()/exp()/exp(

    uxK

    K

    HSRP

    uxKuxKKKK

    LKuxKKKLK

    uxKuxKKK

    LK

    uxKuxKKK

    LKuxK

    a

    a

    B

    ar

    rra

    rdd

    a

    ar

    rdd

    aN

    Na

    NoN

    arra

    od

    ao

    +

    +

    +=

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    Artificial ReaerationOpen water bodies (direct transfer,turnover, fountains)

    Hydropower stations (inject to turbine

    intake, downstream aeration)