dissolved oxygen (do) - philadelphia university · biochemical oxygen demand (bod) : - is the...
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Section VIII Water Treatment- Introduction
Dissolved Oxygen (DO):
- The source of D.O in water is photosynthesis and aeration
- It is one of important parameters to measure the water quality.
- It gives pleasure taste to water
- As the temp D.O
- If the D.O concentration decreases to less than 4mg/l all fish die
- If the D.O concentration is less than 2 mg/l all organism dies and the water is
called septic water
- Best D.O concentration is between 8-10 ppm. Optimum is 9ppm.
- The maximum naturally accrued is 14 mg/l.
Section VIII Water Treatment- Introduction
Biochemical Oxygen demand (BOD) :
- is the quantity of oxygen that is used by microorganism to stabilize the wastewater,
Usually measured after 5 days.
- a BOD test can be used to measure waste loadings to treatment plants, plant
efficiency and the effects of a discharge on a receiving stream, and to control the
plant process.
- It is indicator for the required aeration amount.
- The main equation describes the process is:
DO + organic matter CO2 + biological growth
- Drinking water usually has a BOD of less than 1 mg/L
- Ordinary domestic sewage may have a BOD of 200 mg/L.
-Any effluent to be discharged into natural bodies of water should have BOD less than
30 mg/L.
Test Summary:
1- The sample is filled in an airtight bottle and incubated at 20 oC for 5 days.
2- The dissolved oxygen (DO) content of the sample is determined before and
after five days of incubation at 20°C
3- and the BOD is calculated from the difference between initial and final DO.
The initial DO is determined shortly after the dilution is made; all oxygen uptake
occurring after this measurement is included in the BOD measurement
Section VIII Water Treatment- Introduction
Calculations:
BOD5 mg/l = (Initial DO - DO5) x Dilution Factor
Dilution Factor =Bottle Volume (300 ml)
𝑠𝑎𝑚𝑝𝑙𝑒 𝑉𝑜𝑙𝑢𝑚𝑒
BOD At any time:
BODt = L(1-10-kt
)…. Or BODt = L(1-exp-kt
)….
Where:
BODt : BOD at any time
L: ultimate bio-oxygen demand
k: oxygen decay constant, [day-1
]
t: time, [days]
However: The BOD reaction rate constant (K) is dependent on the following:
1. The nature of the waste:
- degradability of the organic matter. For example , Simple sugar
and starches are rapidly degraded
2. The ability of the organisms in the system to utilize the waste
3. The temperature
- the water temperature may vary from place to place for the same river; hence, the
BOD rate constant is adjusted to the temperature of receiving water using
following relationship:
KT = K20 θ (T-20)
Where
T = temperature of interest, oC
KT = BOD rate constant at the temperature of interest, day-1
K20 = BOD rate constant determined at 20oC, day
-1
θ = temperature coefficient. This has a value of 1.056 in general and 1.047 for higher
temperature greater than 20oC
Section VIII Water Treatment- Introduction
BOD incubator
Example:
Determine ultimate BOD for a wastewater having 5 day BOD at 20oC as 160 mg/L.
Assume reaction rate constant as 0.23 per day (base exp).
Solution
BOD5 = Lo ( 1 – exp-k.t
)
160 = Lo (1 – exp-5 x 0.23
)
Therefore, Lo = 234.1 mg/L
Example:
A BOD test is done by pipiting 5 ml of waste water into 300 ml testing bottle. If the
initial DO was 8.4 mg/l and the DO after 5-days of incubation at 20 oC was 3.7mg/l,
calculate the BOD and estimate the 20-days BOD value assuming the reaction decay
constant k = 0.1 day-1
. (USE base 10)
Solution:
Dilution factor = 300/5 = 60
BOD5 = (8.4 – 3.7)*60 = 282 mg/l ….*
b- to determine the BOD after 20 days:
from (*) calculate L
Section VIII Water Treatment- Introduction
282 = L (1-10−0.1 ×5 ) L = 412 mg/l
Thus BOD20 = 412 (1-10−0.1 ×20 ) BOD20 = 407.8 mg/l
Try the solution using Base (Exp ) but in this case the K = 0.23 day-1
Example:
The wastewater is being discharged into a river that has a temperature of 15oC. The BOD
rate constant determined in the laboratory for this mixed water is 0.12 per day. What
fraction of maximum oxygen consumption will occur in first four days? (Base Exp)
Solution
Determine the BOD rate constant at the river water temperature:
K15 = K20 (1.056) (T-20)
= 0.12 (1.056) (15-20)
= 0.091 per day .....
note 1: per day mean day-1...
note 2: as the temp decrease the reaction rate (K) decreases
Using this value of K to find the fraction of maximum oxygen consumption in four days:
BOD4 = Lo (1 – e-0.091x4
)
Therefore, BOD4 / Lo = 0.305
Section VIII Water Treatment- Introduction
Chemical oxygen demand (COD):
-Measure the amount of organic compounds in water that can be oxidized by strong
oxidant like mixture of sulfuric and chromic acids.
-Most applications of COD determine the amount of organic pollutants found in
surface water.
- It indicates of the strength (degree of pollution) of industrial WW that are not
biodegradable
- the test is faster than BOD test.
PH
- Very important parameter that affects treatment processes, especially
coagulation, anddisinfection
- any unusual change may reflect a major event
H2O H+ + OH
-1,
A- kw = [H+] [OH
-1];;;; kw = 1 × 10−14
B- PH = -log[H+] [H
+] = 10
-PH
Section VIII Water Treatment- Introduction
Conventional water treatment:
is a combination of coagulation, sedimentation, filtration and disinfection process.
1- Primary treatment involves : pumping, screening and grit removal
- Screening: aims to remove large objects, such as stones or sticks, that could
plug lines or block tank inlets.
- grit chamber- slows down the flow to allow grit to fall out
- sedimentation tank (settling tank or clarifier)- settleable solids settle out and
are pumped away, while oils float to the top and are skimmed off
2- Secondary treatment : can remove up to 90% of the organic matter in
wastewater by using biological treatment processes. It performed by attached
or suspended growth processes.
A- Activated Sludge: is the most common option with aeration and agitation, then
allows solids to settle out.
- Bacteria-containing “activated sludge” is continually recirculated back to the
aeration basin to increase the rate of organic decomposition.
B- Trickling Filter: is bed of coarse media (often stones or plastic) 3-10 ft.
deep.
- Wastewater is sprayed into the air (aeration), then allowed to trickle through
the media.
- Microorganisms, attached to and growing on the media, break down organic
material in thewastewater.
- Trickling filters drain at the bottom
C- Lagoons: These are slow, cheap, and relatively inefficient, but can be
used for various types of waste water.
- They rely on the interaction of sunlight, algae, microorganisms, and oxygen
(sometimes aerated).
Section VIII Water Treatment- Introduction
3- Tertiary treatment as ultra filtration
Aerobic conversion of organic matter: the general simplified equation is
C6H12O6 + 6O2 6CO2 + 6H2O + energy
In reality there are more complex equations.
Un-aerobic conversion
Section VIII Water Treatment- Introduction
C6H12O6 3CH4 + 3CO2 + energy + bio mass
It is two step reaction (i) Acidogenic phase where the organic matter converted to
organic acids (ii) Methanogenic phase where organic acids are concerted into methane
and carbon dioxide.
The typical function of each water treatment units can be summarized as the
following:
Treatment unit Function (removal)
Screening Floating matter
Sedimentation Suspended matter
Coagulation Small suspended matter, part of colloid and
bacteria
Filtration Remaining colloidal , dissolved matter and
bacteria
Softening Hardness
Chemical treatment Iron, manganese, heavy metals..etc
Aeration Color, Odor and taste
Disinfection Pathogenic bacteria, organic matter
The type of treatment required for various water sources are as the following:
Water source Recommended treatment
Ground and spring water fairly free from
contamination
No treatment or chlorination
Ground water with chemical, minerals
and gasses
Aeration, coagulation (if necessary)
filtration and disinfection
Lake, surface water reservoirs with low
amount of pollution
Disinfection
Other surface water such as river, canals
and impounded reservoirs with
considerable amount of pollution
Complete treatment
Section IX Water Treatment - Aeration
Aeration:
- It removes odor, color and taste due to reducing the concentration of volatile
gasses like H2S (hydrogen sulfide) , and algae and other related organisms.
- It oxidizes iron and manganese, increases [DO], removes CO2 , CH4 and other
flammable gasses, reduces corrosion.
- Its work principle is based on the fact that the atmospheric oxygen will replace
the volatile gasses in water , while it will escape into atmosphere.
- The replacement will continue till reaching the equilibrium depending on the
partial pressure of each specific gasses.
Type of aeration:
1- Gravity aerators:
In this type water is allowed to fall by gravity, such that large area of water will
exposed to atmosphere.
2- Fountain (Spray) aerators
A special nozzle is used to produce a fine spray. Each nozzle is 2.5- 4cm diameter.
Discharging about 18-36 L/h
Nozzle spacing should be such that each meter cube of water (m3) has aerator area of
0.03 – 0.09 m2 for one hour.
3- Injection or Diffused aerator :
- It consists of tank with perforated pipes, tube or diffuser plates, fixed at the
bottom to release fine air bubbles from compressor unit.
- The tank depth is 3-4m and the tank width is 1.5 times of tank depth.
- If the depth is more the diffusers must be placed at 3-4m below the water
surface
Section IX Water Treatment - Aeration
- Aeration time is 10-30 min and 0.2-0.4 litter of air is required per litter of
water.
- Increase the diffuser depth increases the aeration rate and efficiency
- Decrease the orifice size increases the aeration rate and efficiency
4- Mechanical aerator:
Mixing paddle as in flocculation are used.
Section IX Water Treatment - Aeration
The puddle may be submerged or at surface.
Section IX Water Treatment - Aeration
Settling (Sedimentation)
it is a type of solid liquid separation process in which a suspension is separated into two phases:
a- Clarified supernatant leaving the top of the sedimentation tank (overflow).
b- Concentrated sludge leaving the bottom of the sedimentation tank (underflow).
Purpose of Settling
To remove coarse dispersed phase. To remove coagulated and flocculated impurities.
To remove precipitated impurities after chemical treatment. To settle the sludge (biomass) after activated sludge process /
tricking filters.
Principle of Settling
Suspended solids present in water having specific gravity
greater than that of water (1) tend to settle down by gravity as soon as the turbulence is retarded by offering storage.
Basin in which the flow is retarded is called settling tank. Theoretical average time for which the water is detained in
the settling tank is called the detention period. Sedimentation tanks are circular or rectangular.
Sedimentation types:
itexist, based on characteristics of particlesa. 1- Discrete or type 1 settlingparticleswhose size, shape, and specific gravitydo not
change over time(has a density (ρ) = 2000 – 2200 kg/m3).
2- Flocculating particles or type 2 settling; particles that change size, shape and
perhaps specific gravity over time(has a density (ρ) = 1030 – 1070 kg/m3).
3- Hindered settling or type 3 settling: blanket sedimentation occrues at Lime
softening sedimentation and Sludge thickeners in water treatment
4- Compressed settling or type 4 settlingoccruesSludge thickeners in water treatment
Section IX Water Treatment - Aeration
Applications in Wastewater Treatment:
1. grit removal
2. suspended solids removal in primary clarifier
3. biological floc removal in activated sludge
Place of Sedimentation in various WW plant:
Or
Section IX Water Treatment - Aeration
For treating hard water to removes flocculated solids. The sedimentation tank comes after the flocculation tank.
Section IX Water Treatment - Aeration
Section IX Water Treatment - Aeration
Section IX Water Treatment - Aeration
Section IX Water Treatment - Aeration
Sedimentation Theory:
If a particle is suspended in water , it initially has 2 forces acting upon it.
The forces of gravity Fg = mg .... but m = ρ . Vp
Thus Fg= g* ρp * Vp
The buoyant force quantified by Archimedes Fb =
Thus Fb= g* ρw * Vp
Once motion has been initiated, a third force is created due to viscous friction that is
drag force Fd
Fd= CD *Ap * ρw * 𝑣𝑠
2
2
Section IX Water Treatment - Aeration
Section IX Water Treatment - Aeration
CD = 24/Re For laminar Re < 1
CD = 24/Re + 3/√Re +0.34 For transitional 104> Re > 1
CD = 0.4 ForturbulentRe > 104
Section IX Water Treatment - Aeration
Sedimentation process:
It is a physical treatment that allows for particles having specific gravity higher than
water to settle under its own weight.
Factor affecting the sedimentation:
1- Water prosperities:
b- Sed. Decreases when water viscosity increase
c- Sed. Decreases when water density increase
d- Sed. Increase when water temp. Increase.
2- Suspended solids concentration, size and shape
3- Detention time: sed. Efficiency increase by increasing the water retention at
the tank , but after time the precipitation is decreased sharply thus the time
should be determined correctly. (2-4hr)
4- Flow velocity: decrease the flow velocity increase the sed. The max.
Allowable velocity in the tank is 0.3 m/sec
5- Tank shape: circular tanks are more efficient for sedimentation
Ideal sedimentation tank:
1- The flow is laminar
2- There are no dead zones
3- The horizontal velocity is constant
4- Good arrangement of inlet and outlet weirs.
Section IX Water Treatment - Aeration