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Transcript of Water Quality
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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
34
56
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
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,
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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
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..
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() ()
.
= 0.224
= 0.3480.224 100
= 0.0124
k= 6 (B/A) Lo = 1/ 6(A)2(B)
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= 6(/)= 6(0.0125/0.224)
= 0.335 /
= 1/6()2()
= 266 /
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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)
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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