Industry Homes Water distribution system Sanitary sewer WWTP treatment Pre-Characteristics Drinking water Standards Treatment Treatment processes Reuse or discharge Standards... Bacter
Trang 1WATER POLLUTION CONTROL
Trang 2Industry
Homes
Water distribution system
Sanitary sewer
WWTP
treatment
Pre-Characteristics
Drinking water Standards
Treatment
Treatment processes Reuse or discharge Standards
Trang 3US Primary Drinking Water MCL in mg/L (partial list)
Inorganic Chemicals
Trang 4Bacteriological limits
US EPA states that “bacterial quality criteria for
drinking water from public supplies require not more
than 1 total-coliform/100 ml as the arithmetic mean of all water samples examined per month, with no more than 4 coliforms/100 ml in any sample if the number of samples
is ≤ 20/month, or no more than 4 per 100 ml in 5% of the samples if the number of samples exceeds 20 per month.
Bouwer, Groundwater Hydrology, McGraw-Hill, 1978.
Number of samples taken
for coliform testing
depends on the
population served by the
treatment facility
Population served Number of samples/month
<100,000 100
<1 million 300
Trang 5Secondary Standard for Drinking Water
Contaminant Level Effects
Foaming agents 0.5 mg/L Aesthetic
Sulfate 250 mg/L Taste, laxative effects
Trang 6Water Treatment Plants (WTPs)
A WTP consists of processes to remove contaminants present in
the water such that produced water is suitable for drinking
Raw water
influent
Produced water Effluent WTP
A flow sheet for the plant shows the sequence of the processes
used:
The design of a WTP depends on (1) the quality of raw water,
(2) the quality of produced water and the (3) capacity of the plant
The capacity of the plant depends on the design period (15-25
yrs), the population served, and the per capita water consumption
Trang 7Contaminant Treatment Process
Large debris Screens
Settalable solids Grit chamber
Suspended solids Coagulation/flocculation/
sedimentation (w/ or w/o filtration)Dissolved solids Desalination
Deficit fluoride Fluoridation
Excess fluoride Defluoridation
Undesirable gases Air Stripping
Organic contaminants Activated carbon
Microorganisms Disinfection
Trang 91 Lime Soda-Ash Method
A precipitation method through which Ca is removed as CaCO3 and Mg is removed as Mg(OH)2
Trang 12Wastewater Treatment
System
Raw wastewater Treated
wastewater
Trang 14Treatment Processes
Primary Treatment
Grit Chamber
Wastewater
influent
Effluent Disinfectant
Screens
Primary Settling tank
Contact tank
Primary treatment removes about 35% BOD and 60% SS
Trang 15Secondary Treatment
Biological treatment
Effluent Contact
Trang 16Advanced Treatment
May include:
Activated carbon to remove organic contaminants.
Filter to capture suspended solids.
Nitrate removal
Trang 17Zakher Wastewater Treatment Plant
Trang 18CIVL270-Maraqa
Trang 19Remove large solids and rags that cause problems if passed through the plant
Grit Removal
Remove 95% of grit and stones, which could result in blockages and abrasive, wear on machinery and pipe works
Trang 20Aeration Tanks
Incoming sewage, “seeded” with active organisms, passed through tanks with surface aerators to provide oxygen for the degradation process and to ensure mixing that would maintain sewage and organisms in suspension.
Settling Tanks
After the aeration process the
activated sludge is allowed to settle, leaving an effluent containing less
than 30 PPM of suspended solids
Trang 21Return Activated Sludge:
Some of the sludge from the
settling tanks is returned to be
mixed with incoming sewage to
the aeration tanks, in order to
seed active organisms into the
process
Aeration tank
Return sludge
Settling tank
Sludge to digesters
To further processes
Filtration:
After secondary settling, treated
wastewater passes through sand
filters to reduce the suspended
solids to about 10 ppm
Trang 22Disinfection
Chlorine gas is injected into
the final effluent before the
effluent is being reused
Residual chlorine content of 1
ppm is the desired final
concentration.
Treated effluent is pumped into an elevated tower about 12 km away from the works The tower supplies the roundabout and roadside
irrigation networks and is also used for irrigation of parks
Overall treatment efficiency
BOD removal =98%
TSS removal =99%