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    CHAPTER 2WATER QUALITY

    Water Quality Standards

    and

    Parameters

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    Content

    PART 1: INTRODUCTION

    i) Beneficial Water Useii) Water Resources

    PART 2:WATER QUALITY

    i) Definitionii) Objectivesiii) Water Quality Parameters

    PART 3: WATER QUALITY PARAMETERS

    i) Physicalii) Chemicaliii) Microbiological

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    PART 1

    INTRODUCTION

    (i) Beneficial Water Use

    (ii) Water Resources

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    Beneficial Water Uses

    Municipal Uses

    A ricultural Uses

    Industrial Uses

    Rural Uses

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    Water Resources

    1. Snow / Rain

    2. Surface Water

    (i) Watershed Management

    (ii) Lake /River /Reservoir(iii) Intake Structure

    (iv) Pump(v) Treatment Facilities

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    Cont.

    3. Imported water

    (i) Transmission Pipeline

    (ii) Treatment Facilities

    4.Groundwater(i) Basin Management

    Natural and artificial recharge

    Quality Control

    (ii) Wells

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    PART 2

    Water Qualityi) Definition

    ii) Objective

    iii) Water quality parameters

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    Water Quality Definition

    Is the technical term that is basedupon the characteristics of water in

    suitable for human consumption and

    for all usual domestic purpose

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    Objective of Water Quality

    To control the discharge of

    pollutants so that water quality is

    not degraded to an unacceptableextent below the natural

    background level

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    Water Quality Parameters

    Are the natural and man-made

    chemical, biological and

    m cro o og ca c arac er s cs orivers, lakes and groundwater.

    It provides important information

    about the health of a water body.

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    Are used to find out if the qualitywater is good enough for drinking

    water, recreation, irri ation and

    Water Quality Parameters

    aquatic life.

    These include chemical, physical

    and biological parameters

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    PART 3WATER QUALITY

    PARAMETERS

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    Water Quality Parameters

    1. Physical 2. Chemical

    arameters

    3. Biological

    parameters

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    Physical Parameters

    This parameters respond to the sense of

    sight, touch, taste orsmell

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    Total Solids (TS)

    TSS (Total Suspended Solids - TSS)

    Dissolved Solids (DS)

    Volatile Solids (VS)

    Volatile Disolved Solids (VDS)

    Unit: mg/l

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    Classification of Solids in Water

    and Wastewater

    Solids

    Suspended (> 1mm)

    Colloid (1mm 0.01mm)

    Dissolved (

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    SolidsFilterable

    Non-filterable

    Settleable

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    Non-settleable

    SolidsVolatile

    Non-Volatile

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    Suspended solids (SS) SS contain

    Organic matters

    Biological Solids

    Inorganic mattersClay (size 2 m)

    Silt (size 2-60 m)

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    Analysis of Solids The following test were obtained for a wastewater taken from a headwork

    to a WTP. All the test were performed using sample size of 50 mL.

    Determine the concentration of total solids (TS), total volatile solids (TVS),suspende solids (SS), volatile suspended solids (VSS), total dissolved

    solids (TDS) and volatile dissolved solids.

    Data:

    Tare mass of evaporating dish = 53.5433 gMass of evaporating dish + residue after evaporation at 105oC =53.5794 g

    Mass of evaporating dish + residue after ignition at 550oC = 53.5625 g

    Tare mass of Whatman GF/C filter after drying at 105oC = 1.5433 g

    Mass of Whatman GF/C filter + residue after drying at 105oC = 1.5554 gMass of Whatman GF/C filter + residue after ignition at 550oC = 1.5476 g

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    Caused by foreign matters such as organics compounds,inorganic salts, bacteria, algae and dissolved gases

    Measurement: Threshold Odor Number (TON)

    Examples:

    (i) addition of ammonia in the pipes(ii)excessive manganese & iron present in the finishedwater.

    ** manganese & iron often found in groundwatersupplies where the overall quality of the water is good butthere is a high amount of soluble salt. These metals thenreact with O2 in the distribution system to produced thereduced and insoluble form of the metal**

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    Taste problems relating to watercould be indicators of changes in

    water sources or treatment rocess

    Inorganic compound such asmagnesium, calcium, sodium, copper,

    iron and zinc are generally detected

    by taste of water.

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    It is due to the presence of dissolved andsuspended matter(metallic ions, chemical

    pollutants, plankton and plant pigments from

    humus and peat). These substance do not threaten stream

    water quality, but indicate INCREASED

    DEVELOPMENT in watershed.

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    Dissolved organic material fromhumic substances generally lend a

    brown or tea color to water

    Dissolved organic material fromvegetation and certain inorganic

    matter may cause color in water

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    Is a measure of the amount of particulate

    matter that is suspended in water. Unit-NTU (Nephlometric Turbidity Unit)

    Water that has HIGH turbidity appears

    . HIGH turbidity can cause INCREASED ofwater TEMPERATURE and DECREASEDDO

    WHY???

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    More suspended particles will absorbmore heat which in turn lowers dissolved

    O2 levels.

    It is because

    Such particles (SS clay, silt, finelydivided organic material, plankton) can

    also prevent sunlight from reaching plants

    below surface hence DECREASE the rateof PHOTOSYNTHESIS.

    So, LESS O2 is produced by plant

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    It is a major factor in determining which

    species are present in the stream Temperature will impacts:

    (i) the rates of metabolism and growth of

    aquat c organ sm(ii) rate of plant photosynthesis

    (iii) solubility of O2 in water[0C,

    DO = 14.6 mg/l; 20C, DO = 9.1 mg/l](iv) organisms sensitivity to disease,

    parasites and toxic materials

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    Cool water tastes better

    Temperature affects rate of chemicaland microbiological reactions

    The most suitable drinking waters are

    consistently cool and do not havetemperature fluctuations of more thana few degrees

    Groundwater and surface water frommountain area generally meet thesecriteria

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    CHEMICAL PARAMETERS

    ()

    pH

    Alkalinit

    Hardness

    Biochemical Oxygen

    Demand (BOD)

    Nitrites and Nitrates

    Chemical Oxygen

    Demand (COD)31

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    Chemical Parameters pH

    It is a measure of the concentration ofhydrogen ions

    The term pH was derived from the

    pH

    manner in which the hydrogen ionconcentration is calculated

    pH scale ranges from 0 to 14. A pH of 7is considered to be neutral.

    Substances with pH of less than 7 areacidic; substances with pH greater than7 are basic

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    pH Continues..

    Affects chemical and

    biolo ical reactions

    pH

    Low pH is corrosive

    High pH cause deposits

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    Example 1

    Calculate the concentration of hydrogen ion (H+) for a water sample with pHof 10.

    pH = -log [H+]

    10 = -log [H+]

    pHContinues

    ..

    , + = ant og -

    = 10-10mol/liter

    Example 2

    Calculate the pH value of a water sample which has hydrogen ion

    concentration of 1 x 10-6.4 mol/liter.

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    Work Example Find the Hydrogen ion

    concentration and thehydroxide ion concentration in

    . .

    Concentration unit mol/L then

    mg/L

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    4.1 = +

    , + = 4.1

    = 104.1 /

    + = 14

    = 144.1 = 9.9

    =

    9.9 =

    , = 9.9

    = 109.9 /

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    Conversionof Unit:

    Mol/L to mg/L

    H+ == atomic weight = 1 g/mol

    OH- == atomic wei ht = 17

    g/mol

    Mol/L (conc. ) x g/mol (atomicwt) x 1000mg/1g = mg/L

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    Hardness- Stream water hardness is the total

    concentration of cations, specificallycalcium (Ca2+ ),magnesium (Mg2+), iron

    Fe2+ man anese Mn2+ in the water.

    - Water rich in these cations is said to behard. Stream water hardness reflects

    the geology of the catchment area.

    - Sometimes it also provides a measure

    of the influence of human activity

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    Hardness For instance, acid mine drainage

    often results in the release of iron intoa stream. The iron producesextraordinarily high hardness is ause u wa er qua y n ca or.

    Hardness is a reflection of the amountof calcium and magnesium enteringthe stream through the weathering ofrock such as limestone (CaCO3).

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    Carbonate hardness

    Source: Combination of Ca and Mg

    ions with ions of CO32-, or HCO3-. These carbonate components can be

    as boiling, or by adding lime When the carbonate components

    settled then the water have become

    soft water.

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    Ca 2+ Mg 2+ HCO3- CO3

    2-+

    Carbonate hardness

    Mg(HCO3)2Ca(HCO3)2 CaCO3 MgCO3

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    Noncarbonate Hardness Source: Combinations of Ca and Mg ions with ions of Cl-, SO4

    2-,

    or NO3-.

    The non-carbonate ions cannot be eliminated by ordinary softening

    methods as done on carbonate hardness.

    Usuall elimination of non carbonate hardness is done chemicall b

    adding softening soda (soda ash or sodium carbonate)

    Total hardness is measured in mg/L CaCO3:

    Mg/L material X = Conc. of X (mg/L) (50 mg CaCO3/meq)

    as CaCO3 (Equivalent wt of X (mg/meq))

    Total Hardness as CaCO3 :

    Total Hardness = Ca2+ + Mg2+

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    +Ca 2+ Mg 2+ Cl- SO42- NO3

    -

    Noncarbonate Hardness

    MgCl2Ca(NO3)2 MgSO4 Mg(NO3)2

    CaCl2 CaSO4

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    KeliatanKeliatan BukanBukan KarbonatKarbonat

    ((NoncarbonateNoncarbonate hardness)hardness)

    Keliatan air dinyatakan dalam unit CaCO3 setara.

    Pengkelasan keliatan: Lembut (soft) 50mg/l CaCO3 setara

    Sederhana keras

    (moderately hard) 50-150mg/l CaCO3

    setara

    Keras (hard) 150-300 mg/l CaCO3 setara

    Sangat keras (very hard) >300 mg/l CaCO3 setara

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    Calculation of Water Hardness Find the equivalent weight (EW) of each of the following:

    Ca2+, CO3

    2-, CaCO3

    .

    Solution:

    EW = atomic or molecular weight / n (valence)units: grams/equivalent (g/eq) or milligrams/milliequivalent (mg/meq)

    For calcium, n=2 (valence or oxidation state in water).Atomic weight = 40.08, therefore the EW is then

    EW = 40.08/2 = 20.04 g/eq or mg/meq

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    ..For carbonate ion (CO3

    2-), the oxidation state of 2- isused for n since the base CO3

    2- can potentially

    accept 2 H+. The molecular weight is 60.01.Therefore,

    EW = 60.01/2 = 30 g/eq or mg/meq

    In CaCO3, n=2 since it would take 2H+ to replace the

    cation (Ca2+) to form carbonic acid, H2CO3. the MWis 100.

    Therefore,EW = 100/2 = 50 g/eq or mg/meq

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    A sample of groundwater has 100 mg/L of Ca2+ and 10

    mg/L of Mg2+. Express it hardness in unit of mg/L as

    CaCO3.

    Solution:

    recalled: Mg/L of X = concentration of X (mg/L) (50 mg CaCO3/meq)

    as CaCO3 (equivalent weight of X (mg/meq))

    1. Convert Ca2+ and Mg2+ to mg/L as CaCO3

    Ca2+

    : MW = 40, n=2, EW=40/2 = 20 g/eq or mg/meqMg2+ : MW = 24.3, n=2, EW=24.3/2 = 12.2 g/eq or mg/meq

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    Cont..

    Now, find the mg/L as CaCO3 of cations

    Ca2+ = 100 (50/20) = 250

    Mg2+

    = 10 (50/12.2) = 41Total Carbonate Hardness = Ca2+ + Mg2+

    = 250 + 41

    = 291 mg/L as CaCO3

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    Alkalinity Is measured to determine the ability of a

    stream to resist changes in pH.

    Alkalinity results from the dissolution ofcalcium carbonate (CaCO3) from limestonebedrock which is eroded during the naturalprocesses of weathering

    Alkalinity values of 20 -200 ppm are commonin freshwater ecosystems. Alkalinity levelsbelow 10 ppm indicate poorly bufferedstreams.

    These stream are the least capable of

    resisting changes in pH, therefore they aremost susceptible to problems which occur asa result of acidic pollutants

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    Kealkalian (Alkalinity) Mengukur kebolehan air menyerap (absorbs) ion

    Hidrogen tanpa melibatkan perubahan pH yang

    ketara.

    Jadi, kealkalian adalah ukuran kapasiti penimbal

    buffer ca acit ba i air.

    spesies Karbonat yang menyumbang kepadaalkaliniti adalah:

    Hydroksil (OH-), Ion Karbonat (CO32-), Ion

    Bikarbonat (HCO3-),

    Alkalinity (mol/L) = [HCO3-] + 2[CO3

    2-] + [OH-] [H+]

    Alkalinity (mg/L as CaCO3) = (HCO3-) + (CO3

    2-) +

    (OH-) (H+)50

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    ,

    Nitrogen is an essential nutrient that is

    required by all plants and animals for the

    formation of amino acids. In its molecular form, nitrogen cannot be usedby most aquatic plants, therefore it must beconverted to another form.

    One such form is ammonia (NH3). Ammoniamay be taken up by plants or oxidized bybacteria into nitrate (NO3) or nitrite (NO2). Ofthese two forms, nitrate is usually by the mostimportant.

    Nitrosomonas Nitrobacter

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    Nutrients Nitrogen is often the limiting nutrient in

    ocean waters and some streams Nitrogen can exist in numerous forms, but

    - - 3 , 2 ,

    (NH3) are most commonly measured

    Sources are primarily from fertilizers and

    acid deposition

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    Biochemical Oxygen Demand

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    Biochemical Oxygen Demand

    (BOD)

    It is a measure of the quantity of oxygen

    used by microorganisms (eg.aerobicbacteria) in the oxidation of organic matter.

    In other words: BOD measures the change

    in dissolved oxygen concentration causedby the microorganisms as they degrade the

    organic matter.

    High BOD is an indication of poor waterquality

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    Biochemical Oxygen Demand

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    Biochemical Oxygen Demand

    (BOD)

    BOD bottles

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    Bi h i l O

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    Biochemical Oxygen

    Demand Measurement Take sample of waste; dilute with

    oxygen saturated water; add nutrientsand microorganisms (seed)

    days Temperature 20 C

    In dark (prevents algae from growing)

    Final DO concentration must be > 2 mg/L Need at least 2 mg/L change in DO over 5 days

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    Example 1 A BOD test was conducted in the

    laboratory using wastewater being

    dumped into Lake Spartan. The

    samples are prepared by adding 3.00

    mL of wastewater to the 300.0 mL BODbottles. The bottles are filled to capacity

    with seeded dilution water.

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    E l 1 R D t

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    Example 1: Raw Data

    Time(days)

    Dilutedsample

    DO (mg/L)

    Blank SeededSample DO

    (mg/L)

    0 7.95 8.15

    1 3.75 8.102 3.45 8.05

    3 2.75 8.00

    4 2.15 7.955 1.80 7.90

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    Example 1: Calculations What is the BOD5 of the sample?

    volumetotalsample/volumefactordilutionP

    PP)])(1B(B-)DO[(DOBOD fifim

    ==

    =

    Plot the BOD with respect to time.samplediluted

    theofionsconcentratDOfinalandinitialDO,DO

    (blank)waterdilutedseededtheofionsconcentratDOfinalandinitialB,B

    fi

    fi

    =

    =

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    Example 1: Time Concentration Plot

    400

    500

    600

    700

    g/L)

    0

    100

    200

    300

    0 1 2 3 4 5 6

    time (days)

    BOD

    (

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    Modeling BOD as a First-order Reaction

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    Modeling BOD as a First-order Reaction

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    6

    mg/L)

    Organic matter oxidized

    0

    1

    2

    0 10 20 30

    time (days)

    Conc

    .

    Organic matter remaining

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    .

    tt - kL

    dL=

    demandoxygenuscarbonaceoultimatetheiswhere

    :yieldsequationthisSolving

    (timeconstantrateBODthe

    ttimeafterleftdemandoxygenofamountwhere1-

    o

    kt

    ot

    t

    L

    eLL

    k

    L

    =

    ==

    )

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    Ultimate BOD

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    Ultimate BOD

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    nc.(mg/L)

    LoLo- Lt BOD exerted

    BODt

    0

    1

    0 10 20 30time (days)

    C

    Lt L remaining

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    Ultimate Biochemical Oxygen

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    yg

    Demand

    Lt = amount of O2 demand left in sample at

    time, tLo = amount of O2 demand left initially (at time 0,

    =,

    At any time, Lo = BODt + Lt (that is the amountof DO demand used up and the amount

    of DO that could be used up eventually)

    Assuming that DO depletion is first orderBODt = Lo(1 - e

    -kt)

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    Example 2

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    p If the BOD5 of a waste is 102 mg/L and the

    BOD20 (corresponds to the ultimate BOD) is

    158 mg/L, what is k (base e)?

    kteL = 10tBOD

    kteL

    =0

    1 tBOD

    ktL

    =

    0

    1ln tBOD

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    Example 2 (cont)

    tLk

    = 0

    1ln tBOD

    day

    mg/Lmg/L

    5

    1581021ln

    =k

    -1day21.0=k65

    Biological Oxygen Demand:

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    Biological Oxygen Demand:

    Temperature Dependence

    Temperature dependence of biochemical

    oxygen demand

    As temperature increases, metabolism

    increases, utilization of DO also increases

    kt = k20T-20

    = 1.135 if T is between 4 - 20 oC

    = 1.056 if T is between 20 - 30 oC

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    Example 3The BOD rate constant, k, was determined

    empirically to be 0.20 days-1

    at 20o

    C.What is k if the temperature of the water

    increases to 25 oC?

    What is k if the temperature of the waterdecreases to 10 oC?

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    Example 3 : Solution

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    Example 3 : Solution

    2025

    25 )056.1(20.0 = -1dayk

    -1da26.0=k

    2010

    10 )135.1(20.0 = -1dayk

    -1day056.010 =k

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    Nitrogenous Oxygen Demand

    So far we have dealt only withcarbonaceous demand (demand to

    Many other compounds, such asproteins, consume oxygen

    Mechanism of reactions are different

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    Nitrogenous Oxygen Demand Nitrification (2 step process)

    2 NH3 + 3O2 2 NO2- + 2H+ + 2H2O2 NO2

    - + O2 2 NO3-

    NH3 + 2O2 NO3- + H+ + H2O

    Theoretical NBOD =

    N/gOg4.5714

    16x4

    oxidizednitrogenofgrams

    usedoxygenofgrams2

    ==

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    Nitrogenous Oxygen Demand

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    Nitrogenous oxygen demand Untreated domestic wastewater

    ultimate-CBOD = 250 - 350 mg/Lultimate-NBOD = 70 - 230 mg/L

    Total Kjeldahl Nitrogen (TKN) = totalconcentration of organic and ammonia

    nitrogen in wastewater: 15 - 50 mg/L as N

    Ultimate NBOD 4.57 x TKN

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    Other Measures of Oxygen

    eman

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    Example 5 Theoretical oxygen demand (ThOD)

    C6H

    12O

    6(glucose) + 6O

    26 CO

    2+ 6H

    2O

    If concentration of glucose is 10 mg/L what is the

    theoretical oxygen demand (amount of DO

    required?)

    LOmg

    glucosemmol

    glucosemg

    Ommol

    Omg

    glucosemmol

    Ommol

    Lglucosemg 22

    22

    7.10180

    326

    10 =

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    Chemical Oxygen Demand Chemical oxygen demand - similar to BOD

    but is determined by using a strongoxidizing agent to break down chemical

    Still determines the equivalent amount ofoxygen that would be consumed

    Value usually about 1.25 times BOD

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    Thomas method: Graphical determination of

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    BOD rate ConstantsAccording to Thomas,

    (1-e-kt) = kt(1+kt/6)-3

    Therefore

    BODt=Lo(1-e-kt)BODt=Lo(kt)[1+(1/6)kt]

    -3 .....(1)

    By rearranging terms & taking the cube root of both sides,equa on can rans orme o:

    (t/BODt)1/3=(kLo)

    -1/3 + (k)2/3/6(Lo)1/3 (t) ....(2)

    A plot of (t/BODt)1/3 versus tis linear. The intercept is

    defined as:

    A = (kLo)-1/3

    .(3)

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    ..

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    ..

    a slope is defined by:B = (k)2/3/6(Lo)

    1/3 .(4)y=(t/BOD) 1/3

    Recalled , y= c + mx

    =

    m=a/b = (k2/3/6Lo1/3)

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    Solving Lo1/3 in Eq.(3) substituting into Eq. (4) and solving for k

    yields:

    k= 6(B/A) (5) Likewise, substituting Eq. (5) into Eq.(3) and solving for Lo yields:

    Lo = 1/6(A)2

    (B) (6)

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    ,

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    ,

    :

    (/) 125 200 220 230 237

    79

    ,

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    ,

    (/)

    1/3

    .

    (/) 125 200 220 230 237

    (/)1/3

    .

    (/)1/3 0.252 0.271 0.301 0.326 0.348

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    0.3

    0.4

    0.5

    = 2/3 1/3

    )

    = 0.224

    0

    2 4 6 8 10

    0.1

    0.2

    =0.0125

    81

    ..

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    () ()

    .

    = 0.224

    = 0.3480.224 100

    = 0.0124

    k= 6 (B/A) Lo = 1/ 6(A)2(B)

    82

    ..

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    = 6(/)= 6(0.0125/0.224)

    = 0.335 /

    = 1/6()2()

    = 266 /

    83

    WATER QUALITY

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    MEASUREMENTThOD theoretical oxygen demand

    (i) It is the amount of O2 required tooxidize a substance to CO2 and H2O

    ii Calculated b stoichiometr if the

    chemical composition of the substanceis known

    (iii) The ThOD of X in mg/L

    = (amount of X in mg/L )( MW of O2 in g/MW of X in g)

    84

    Example:

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    Compute the ThOD of 108.75 mg/L

    of glucose (C6H12O6) STEPS:

    wr e a ance equa on or e

    reaction

    (ii) Compute the grams molecular

    weights of the reactants(iii) Determine ThOD

    BFC 3103

    ENVIRONMENTAL ENGINEERING85

    Example:

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    The balanced equation for the reaction

    C6H12O6 + O2 CO2 + H2O

    The molecular weights (grams) of thereactants

    Oxygen =Thus, it takes ? of O2 to oxidize ? g of

    glucose to CO2 and H2O.

    The ThOD of 108.75 mg/L of glucose is(108.75 mg/L glucose)( ? g O2/ ? g

    glucose) =116 mg/L O286

    Example:

    Th b l d ti f th ti

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    The balanced equation for the reaction

    C6H12O6 + 6O2 6CO2 + 6H2O

    The molecular weights (grams) of the reactants

    Glucose = 6C=72, 12 H=12, 6O=96, = 180

    Oxygen =6(2)O=192

    Thus, it takes 192 of O2 to oxidize 180 g of

    glucose to CO2 and H2O.

    The ThOD of 108.75 mg/L of glucose is

    (108.75 mg/L glucose)(192 g O2/180 g glucose)

    =116 mg/L O2

    87

    Exercise

    (5 1 5 2 5 3 i th t t b k)

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    (5.1, 5.2, 5.3-in the text book)

    1. Glutamic acid (C5H904N) is used as one of

    the reagents for a standard to check the BOD

    test. Determine the ThOD of mg/L of glutamic

    acid. Assume the following reaction apply:

    C5H904N + 4.5O2 5CO2 + 3H2O + NH3

    NH3 + 2O2 NO3+ H+ + H2O

    88

    Pathogenic Organisms

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    Many organims that cause human oranimal diseases colonize the instinal tract

    but can live for a period of time outside thebody

    disease symptoms) excrete theseintestinal tract organims in very largenumbers

    When water is contaminated by excretia,the organisms can be transmitted to thosewho contact the water

    89

    Pathogenic Organisms

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    90

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    91

    Classification of Water

    A i t d Di

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    Associated Diseases

    92

    Disease Rates and Risk

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    93

    Biological Parameters

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    It is biomonitor: defined as an organism

    that provides quantitative information on

    the quality of the environmental around

    it.

    It can be deduced through the study ofthe content of certain elements or

    compounds, morphological or cellular

    structure, metabolic-biochemicalprocess behavior or population structure

    94

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    .. There are several types of bioindicators:

    (i) plant indicators

    - the presence or absence of certain plant or othervegetative life in an ecosystem can provide important

    - lichens are organism comprising both fungi and algae.

    Lichens are found on rocks and tree trunks, and theyrespond to environmental changes in forest, includingchanges in forest structure conservation biology, airquality and climate

    - The disappearance of lichens in a forest may indicateenvironmental stresses, such as high level of sulfurdioxide, sulfur-based pollutants and nitrogen oxides

    95

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    Lichens

    96

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    (ii)Animal indicator and toxins- an increase or decrease in an animal

    population may indicate damage to theecosystem caused by pollutant. For eg; ifpopulation causes the depletion ofim ortant food sources animal s eciesdependent upon these food sources will

    also be reduced in number: populationdecline- Submerged aquatic vegetation (SAV)

    provides invaluable benefits to aquaticecosystems. It not only provides food andshelter to fish and invertebrates but alsoproduces oxygen, trap sediment andabsorbs nutrients such as nitrogen andphosphorus

    97

    Cont

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    Cont(iii) Microbial indicators and chemical

    pollutants

    - Microorganisms can be used asindicators of aquatic or terrestrialecosystem health

    - Found in large quantities, microorganism

    will produce new proteins, called stressproteins when exposed to contaminantslike cadmium and benzene

    - These stress proteins can be used as anearly warning system to detect highlevels of pollution

    BFC 3103

    ENVIRONMENTAL ENGINEERING98

    Cont

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    Cont(iv) Macroinvertebrate bioindicators- Macroinvertebrate are useful and

    convenient indicators of the ecologicalhealth of a waterbody or river. They arealmost alwa s resent and are eas tosample and identify

    - Benthic refers to the bottom of awaterway. Example of benthicmacroinvertebrates include insects intheir larval or nymph form, crayfish,

    claims, snails and worms. Most live partor most of their life cycle attached tosubmerged rocks, logs and vegetation.

    99

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    BFC 3103

    ENVIRONMENTAL ENGINEERING

    Macroinvertebrata

    100

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    101

    Cont

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    Cont- The basic principle behind the

    study of macroinvertebrates is that

    some are more sensitive topollution than others

    - Therefore, if a stream site isinhabited by organism that cantolerate pollution and the morepollution-sensitive organisms are

    missing a pollution is likely

    102

    Microbiological

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    Microbiological

    Bacteria( coliform test)

    Virus

    Algae

    103

    Bacteria

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    Bacteria Pathogenic bacteria causing cholera,

    typhoid fever etc

    Indicator bacteria

    o orm

    Fecal Coliform( E. Coli)

    104

    Virus

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    Virus One virus can cause

    illness

    Hard to detect

    pec y rea men

    process ( disinfectiondose and contact time)

    instead of measuring

    virus concentration

    105

    Algae

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    Algae Taste and odor

    Some algae could be harmful to animals fish

    r s

    BFC 3103

    ENVIRONMENTAL ENGINEERING106

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    EFFECTS ON WATER

    QUALITY

    2) Nontoxic organic3) Toxic organic

    107

    Toxic inorganic elements and

    radicals

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    radicals Arsenic, Mercury, Cadmium,

    Chromium, Lead-- accumulates in

    body

    Nitrate--Blue baby Perchlorate ( ClO4

    -) --Thyroid

    disorder, cancer

    108

    Nontoxic organics

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    Nontoxic organics NOC ( Natural organic matter)

    Decayed vegetation etc

    Form toxic disinfection by-products

    Lower concentrations up to 4 mg/lmay be removed by Enhanced

    Coagulation.

    109

    Toxic organics

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    Toxic organicsCausing cancer, mutation or

    miscarriage

    chlorinated hydrocarbons

    orop enoxy er c es

    Trihalomethanes

    VOCs and SOCs.

    110

    Other Contaminants

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    Other Contaminants Asbestos

    Radionuclides Alpha and Beta radioactivity

    ran um, a um, a on

    111

    Dissolved oxygen (DO)It i ti l f th i l f

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    yg ( ) It is an essential for the survival of

    nearly all aquatic life and measured

    in mg/L If oxygen levels are high, it was

    presume that pollution levels in the

    water are low. Conversely, if oxygen levels are low,

    one can presume there is a high

    oxygen demand and that the body ofwater is not of optimal health

    112

    Cont

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    Levels of DO vary depending on factorsincluding water temperature, time of day,

    season, depth, altitude and rate of flow.(i) water at higher temp and altitudes will haveLESS DO. so, demand O2 will increased

    ecause a g er emp, e ra e o

    metabolisme is increased.(ii) at night, DO decreased as photosynthesishas stopped while oxygen consumingprocess such as respiration, oxidation

    (iii) DO reaches its peak (HIGH) during theday

    113

    DO sag curve

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    The concentration of DO in a river is an

    indicatorof the general health of the river.

    All rivers have CAPACITY for self purification.(i) As long as the discharge of oxygen

    purification capacity, the DO level remain HIGH

    and a diverse population of plants and animals

    (ii) As the amount of waste increase, the self

    purification capacity can be exceeded, causing

    detrimental changes in plant and animal life

    114

    .(iii) then the stream losses its ability to clean

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    (iii) then, the stream losses its ability to cleanitself and the DO level DECREASES.

    (iv) when the DO drops below 4 to 5 mg/L,most game fish will have been driven out.

    ,other higher animals are killed or driven

    (v) The water become blackish and foulsmelling as the sewage and dead animal lifedecompose under anaerobic condition

    (without O2)

    BFC 3103

    ENVIRONMENTAL ENGINEERING115

    Dissolved Oxygen Depletion

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    (From: Environmental Science: A Global Concern, 3rd ed. by W.PCunningham and B.W. Saigo, WC Brown Publishers, 1995)

    116

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    117

    Mass Balance Approach

    O i i ll d l d b H W St t d

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    Originally developed by H.W. Streeter and

    E.B. Phelps in 1925

    River described as plug-flow reactor

    ass a ance s s mp e y se ec on o

    system boundaries Oxygen is depleted by BOD exertion

    Oxygen is gained through reaeration

    118

    Steps in Developing the DO

    Sag Curve

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    1. Determine the initial conditions

    2. Determine the reaeration rate from streamgeometry

    3. Determine the deoxygenation rate from

    BOD test and stream geometry

    4. Calculate the DO deficit as a function of

    time

    5. Calculate the time and deficit at the critical

    point

    119

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    120

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    Qw = waste flow (m3/s)DOw = DO in waste (mg/L)

    Qr= river flow (m3/s)

    DOr= DO in river (mg/L)

    Lr= BOD in river (mg/L)

    Qmix = combined flow (m3/s)

    DO = mixed DO (mg/L)

    La = mixed BOD (mg/L)

    w

    121

    1.

    a. Initial dissolved oxygen concentrationDOQDOQ +

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    b. Initial dissolved oxygen deficit

    rw

    rrww

    QQ

    DOQDOQDO

    +

    +=

    where D = DO deficit (mg/L)

    DOs = saturation DO conc. (mg/L)

    mix

    rrwwsa

    Q

    DOQDOQDOD +=

    s

    122

    1. Determine Initial Conditions

    DO t is a function of temperature Values

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    DOsat is a function of temperature. Values

    can be found in Table A-2.

    c. Initial ultimate BOD concentration

    rw

    rrwwa

    QQ

    L

    +

    +=

    123

    2. Determine Reaeration Rate

    a. OConnor-Dobbins correlation2/19.3 u

    k

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    where kr= reaeration coefficient @ 20C (day-1)

    u = avera e stream velocit m/s

    2/3hkr=

    h = average stream depth (m)

    b. Correct rate coefficient for stream temperature

    where = 1.024

    20

    20,

    = Trr kk

    124

    . = kdLt

    kd

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    kd

    (1)

    Lt

    . kd

    () = k( )

    tk

    tdeLL

    = 0

    tk

    ddeLk

    = 0tiondeoxygentaofrate125

    3. Determine the Deoxygenation Rate

    c. However, k= kd only for deep, slow moving

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    , d y p, gstreams. For others,

    hukkd +=

    where = bed activity coefficient (0.1 0.6)

    d. Correct for temperature

    where = 1.135 (4-20C) or 1.056 (20-30C)

    20

    20,

    = Trr kk

    126

    4. DO as function of time

    Mass balance on moving element

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    g

    DkLkdt

    dDrtd

    =

    ( ) ( )tkatktkdr

    adt

    rrd eDeekk

    LkD +=

    127

    5. Calculate Critical time and DO

    drr kkD

    k1l

    1

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    =

    ad

    dra

    d

    r

    dr

    cLk

    Dkkk

    t 1ln

    ( ) crcrcd tk

    a

    tktk

    ar

    ad

    c eDeekk

    Lk

    D

    +=

    128

    Example

    A city of 200,000 people discharges 37.0cfs of treated sewage having an ultimate

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    BOD of 28.0 mg/L and 1.8 mg/L DO into a

    river with a flow of 250 cfs and velocity of1.2 ft/sec. U stream of the dischar e

    point, the river has a BOD of 3.6 mg/L and

    a DO of 7.6 mg/L. The saturation DO is8.5 mg/L, kd = 0.61 day

    -1, and kr= 0.76

    day-1. Determine a) the critical DO and

    critical distance, and b) the DO at 10 miles

    downstream.129

    1. Determine Initial Conditions

    a. Initial dissolved oxygen concentration

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    rw

    rrww

    QQ

    DOQDOQ

    DO +

    +

    =

    b. Initial dissolved oxygen deficit

    DODOD s=

    L

    85.6

    37250

    ...=

    +

    +=DO

    L

    mg6.185.65.8 ==aD

    130

    1. Determine Initial Conditions

    c. Initial ultimate BOD concentration

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    rw

    rrwwa

    QQLQLQL

    +

    +=

    ( )( ) ( )( )Lmg75.6

    37250

    2506.30.3728 =++=aL

    131

    Step 1. Variations

    Flow given in cfs, not m3/s does not

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    g

    matter for mixing calculations

    Saturation DO given no need to look up

    ma e g ven no nee o ca cu a e

    from BOD5

    132

    2. Determine Reaeration Rate

    kr = 0.76 day-1 given

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    r y g

    no need to calculate from stream

    geometry

    assume g ven va ue s a e s ream

    temperature (since not otherwisespecified), so no need to correct

    133

    3. Determine the Deoxygenation Rate

    kd = 0.61 day-1 given

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    d

    no need to calculate corrections from

    stream geometry

    assume g ven va ue s a e s ream

    temperature (since not otherwisespecified), so no need to correct

    134

    5. Calculate Critical time and DO

    = drrkk

    Dk

    t 1ln1

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    =

    ad

    a

    ddr

    cLk

    Dkkk

    t 1ln

    ( )( )

    =

    75.661.0

    ..6.11

    61.0

    .ln

    61.076.0

    ct

    day07.1=ct

    135

    5. Calculate Critical time and DO

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    ( )

    = ft

    midhr

    hrs

    sftd

    528012436002.107.1cx

    mi9.20=c

    x

    136

    5. Calculate Critical time and DO

    ( ) tktktkad DLkD

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    ( ) crcrcd tkatktkar

    adc eDee

    kk

    D +

    =

    ( )( ) ( )( )

    ( )( )( )07.176.0

    07.176.007.161.0

    6.1

    61.076.0

    ..

    +

    =

    e

    eeDc

    L

    mg58.2=cD137

    5. Calculate Critical time and DO

    csc DDODO =

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    mg7.558.25.8 ==cDO

    138

    4. DO as function of time (at 10 miles)

    ( )ft

    mi 528010

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    ( )

    dhrsft

    mimi

    miles10 51.0

    528010

    =

    =t

    dhrs.

    ( )( ) ( )( ) ( )( )( )( )( )07.176.0

    07.176.007.161.0

    6.1

    61.076.0

    75.661.0

    +

    =

    e

    eeDc

    139

    4. DO as function of time (at 10 miles)

    mg582D

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    L

    gmiles10 58.2=D

    Lmiles10 9.558.25.8 ==DO

    140

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    141

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    142