SUBJECT- ENVIRONMENTAL ENGINEERING
CSMSS CSCOE,AURANGABAD
1
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
MODULE - 2
TREATMENT OF WATER
2
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
CONTENT
 CONVEYANCE OF RAW WATER PIPELINES AND CANALS
 DESIGNING OF RISING MAINS
 TYPE OF VALVES
 TYPE OF PUMPS
 INTAKE STRUCTURE
 TREATMENT OF WATER
 AERATION
 SEDIMENTATION
 COAGULATION
 RAPIT MIXING
 CLARIFLOCCCULATOR
 DESIGN CRITRRIA FOR FLOCCULATION BASIN USING
ROTATION PADDLES
 PLATE SETTLER
3
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
CONTENT
 TUBE SETTLER
 FILTRATION
 TYPESOF FILTERS
 DISINFACTION
 REQUIREMENT OF AN IDEAL DISINFACTANT
 MECHANISM OF DISINFACTION
 WATER SOFTENING METHODS
 DEMINERALISATION/DEIONIZATION
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.1CONVEYANCE OF RAW WATER
PIPELINES AND CANALS
 2.1.1.Pipelines
 2.2.2.Aqueducts
(Open channels)
 2.1.3.Advantages of Pipelines and Aqueduct
Systems
 2.1.4 Disadvantages of Pipelines and Aqueduct
Systems
 2.1.5 Hydraulics of Conduits
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.1.5 Hydraulics of Conduits
 Fluid Flows
1.Classification Based on Variation with time
2. Classification Based on Variation with space
 Flow Type & Examples
A steady flow can be uniform or non-uniform and
similarly an unsteady flow can also be uniform or
non-uniform.
For steady flow discharge is constant with time and
for a uniform flow the area of cross section of the
fluid flow flow is constant through the flow path.
6
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.1.6 Laying of Pipes
7
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.1.7 Joints in Pipes
1.Joints in Cast Iron Pipes
(a)Bell and Spigot Joint
8
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
(b)Expansion Joint (c)Flanged
Joint
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.Joints in Concrete Pipes
(a)Cement Collar Joint (b)Simplex
Joint
10
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.1.8.Testing of Pipelines
 A Pipeline section about 300 m length is tested
for leakage, strength etc.
1.Pressure Test
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
 2.Leakage Test
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.2DESIGNING OF RISING MAINS
2.2.1 RISING MAINS
The water, after pumped, is taken to the high levelled
gravity pipe through the rising main.
 The rising main may be of cast iron or asbestos cement
pressure pipes.
 The velocity of flow in the rising main should not be less
then 0.75 m/sec. at any time of flow.
2.2.2 DESIGN STEPS
Following are the step for design of the rising main.
STEP 1:Assume the velocity of flow in the rising main.
STEP 2:Determine required cross-sectional area of the
rising main.
STEP 3: 2:Determine required diameter of rising main.13
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.3 TYPE OF VALVES
 The fixtures which are fixed along the distribution
system are know as valves.
 PURPOSES SERVED
1.Control the rate of flow of water.
2.Releases or admits air into the pipeline.
3. Prevents or detects leakage.
4.Meets the demand during emergencies.
5.Make the distribution system more efficient.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.3.1 SLUICE VALVE.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.3.2 AIR RELIEF VALVE
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.3.3.PRESSURE RELIEF
VALVE
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.4 TYPE OF PUMPS
 2.4.1Gear Pumps
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
 2.4.2 Rotary Vane Pumps
 2.4.3Screw Pumps
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
 2.4.4 Bent Axis Pumps
 2.4.5 Inline Axis Pumps
20
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
 2.4.6 Radial Piston Pumps
21
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.5 INTAKE STRUCTURE
 The raw water required for any water supply
scheme is withdrawn from a surface source like
river, reservoir, lake or canal, or from underground
source like well or spring.
 When the withdrawal of water is from surface
source, a constriction called intake structure is
provided to collect fluctuating levels, and discharge
it into pipe.
 Intake structure mainly consist of:
1) Conduit with protective works,
2) Screens at open ends
3) Gates and valves to regulate the flow, and
22
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.5.1 FACTORS GOVERNING THE
LOCATION OF INTAKE
 It should be near the treatment plant to cut down the cost
of conveyance.
 It should be located in the comparatively pure zone of
water source to reduce the load on treatment work.
 It should not be located on the downstream side of the
sewage disposal.
 It should not be located on curves.
 It should be located at such a site from where it can draw
water even during driest period of year.
 It should be away from navigation channels as it may
admit raw water polluted by discharge of wastes by
ships.23
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.5.2 TYPES OF INTAKES
 1.SUBMERGED OR LAKE INTAKE
 2.EXPOSED INTAKES
A) Canal Intake.
B) Reservoir Intake.
 3.RIVER INTAKE.
 4. MOVEBLE INTAKE
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
1.SUBMERGED OR LAKE INTAKE
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.EXPOSED INTAKES
A) Canal Intake.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
B) Reservoir Intake.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
3.RIVER INTAKE.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
4. MOVEBLE INTAKE
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.6 TREATMENT OF WATER
2.6.1 Necessity of Treatment of Water
 The following are the objectives of treatment of water.
 To make water odour free and tasty.
 To make the water safe and sparkling for drinking and
domestic purposes.
 To make it colourless.
 To remove dissolved gases and turbidity of water.
 To make it free from all objectionable impurities
present in suspension, colloidal or dissolved from.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
 To remove harmful bacteria.
 To remove hardness of water.
 To make the water suitable for a wide variety of
industrial purposes like dyeing, brewing, soft
drinks, steam generation etc.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.6.2.LAYOUT AND
COMPONENTS OF WATER
TREATMENT PLANT
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD33
2.7 AERATION
 The process of exposing large surface of water to
the atmospheric air is called aeration.
 Its main purpose is to absorb more oxygen and
let out unpleasant odours and gases and oxidise
Fe and Mn in water.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.7.1 Objectives of Aeration
 To increase oxygen contents in water for
imparting freshness.
 To expel volatile substances and gases like
H2S,CO2,causing bad taste and odour.
 To oxidize iron and manganese so that these can
be precipitated and removed.
 To destroy bacteria to some extent, by agitation of
water during aeration.
35
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.7.2 METHODS OF
AERATIONS
1.By Using Fountains, Spray Nozzles.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.Gravity or Free Fall Aerators.
(a)Cascade Aerators:
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
(b)Inclined Apron Aerator:
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
3.Trickling Beds or Multiple Trays.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
4.BY AIR DIFFUSION
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
EXAMPLES
 The maximum daily demand of water is 114 MLD.
Design aeration fountain(cascade aerator).
Solution:
Q=114MLD
(i) Diameter of bottommost cascades:
Design flow, Q= 114MLD
= 114 X 106 Lit/day
= 4750 m3/hr.
Loading rate= 0.03m2/m3/hr.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD43
2.8 SEDIMENTATION
 Principle of sedimentation is applied for the
removal of
(i) Grit in grit chamber
(ii) Destabilized floc in clariflocculators,
(iii) Particulate matter in primary and secondary
settling basins.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.8.1 TYPE OF
SEDIMENTATION
1.PLAIN SEDIMNETATION
(Settling velocity of a discrete particle depends upon
specific gravity and diameter of the particle,
gravitational acceleration and kinematic viscosity)
2. SEDIMENTATION WITH COAGULATION OR
CHEMICALLY ASSISTED SEDIMENTATION
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.8.2 Type of Sedimentation
Tanks
 1.Fill and Draw Type.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.Continuous Flow Tank
(a) Horizontal Flow Type:
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
(b)Vertical Flow Type:
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.9 COAGULATION
 The process of mixing certain chemicals to water to neutralize the
electrical charges and to form an insoluble, gelatinous flocculent
precipitate for absorbing and entraining suspended and colloidal particles
of impurities is called coagulation.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Factor affecting Coagulation
 Type of coagulant
 Dose of coagulant
 Time and method of mixing the coagulant.
 Character of water
1. Ph of water
2. Temperature of water
3. Nature and quantity of suspended matter.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.9.2. Coagulation process
 Following processes
1. Feeding
2. Mixing
3. Flocculation
4. Clarification or sedimentation.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
By toothed wheel By helical screw
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD52
1. Feeding- a)Dry feeding
B) Wet feeding
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD53
 Mixing
In order to cause the complete dispersion of the
added coagulant into the entire mass of water,
mixing devices are required.
The violent agitation of water can be achieved by
using mixing devices like compressed air,
centrifugal pumps and mixing basins.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD55
 Compressed air device.
(By passing compressed air from bottom surface of
mixing basin)
 Centrifugal pump.
(There will be efficient dispersion of coagulant in water
while passing through the impeller of pump.)
 Mixing channel with flume.
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD56
 Mixing basin with baffle walls.
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD57
 Mixing basin with mechanical devices
 Flocculation
In colloid chemistry, flocculation refers to the process
by which fine particulates are caused to clump together
into a floc. The floc may then float to the top of the liquid
(creaming), settle to the bottom of the liquid
(sedimentation), or be readily filtered from the liquid.
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CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD59
 Clarification or sedimentation.
After flocculation water is admitted into basins called
clarifiers or settling basins.
Water is detained in a such tank for a detention
generated under flocculation, settles down in the
form of sludge
The clear water taken out through outlet
arrangements and generally admitted to filtration
tanks for further purification.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD61
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD62
2.9.4 Common Coagulants
Following common coagulants are used:
1. Alum or aluminum sulphate.
2. Chlorinated copperas
3. Magnesium carbonate and lime
4. Ferrous sulphate and lime
5. Sodium aluminate
6. Polyelectrolytes.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.11 CLARIFLOCCULATOR
 Clariflocculator is a combination of flocculation and
clarification in a single tank. It has two concentric
tanks where inner tank serves as a flocculation basin
and the outer tank serves as a clarifier.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD65
2.15 FILTRATION
 Filtration is the process of separating suspended solid
matter from a liquid, by causing the latter to pass
through the pores of some substance, called a filter.
The liquid which has passed through the filter is called
the filtrate.
 Filtration is a process of removing particulate and
bacterial impurities which could not be removed in
earlier processes, from water by passing it through a
porous medium.
 It is an important stage in the purification of water.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.15.2 FILTER MATERIALS
 Sand
 Anthracite
Anthracite, often referred to as hard coal, is a hard,
compact variety of coal that has a sub-metallic luster. It
has the highest carbon content, the fewest impurities, and
the highest energy density of all types of coal and is the
highest ranking of coals.
[ Carbon content (%): 92 – 98]
 Garnet sand or limonite
 Locally available materials
 Gravel
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.16 TYPE OF FILTERS
2.16.1 SLOW SAND FILTER
The filter media is supported by this base material
LAYER SIZE OF GRAVEL
First layer(Bottom) 40 TO 65 mm
Second layer 20 TO 40 mm
Third layer 6 TO 20 mm
Fourth layer(Topmost) 3 TO 6 mm
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
2.16.2 RAPID SAND FILTER OR
MECHANICAL SAND FILTER.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD71
2.17 DISINFECTION
 Disinfection is a process of killing all pathogens.
 Sterilization is a process in which the total and
complete destruction of all types of bacteria takes
place.
 Theory of Disinfection
Safe water means
1.Water free from bacteria.
2.Water aesthetically acceptable.
3.Water free from excessive minerals and
poisonous matter.
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
Factors affecting the efficiency of
disinfection.
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD73
 Nature and concentration of organisms.
 Nature and concentration of disinfectant.
 Temperature of water.
 Time of contact
 Nature of physical agent.
 Nature of water to be disinfected.
 pH of water.
Disinfecting agents.
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD74
1.Physical agents.
 Heat
 Light (natural sun radiation, artificial)
2.Chemical agents.
 Potassium permanganate (used in hospitals)
 Ozone
 Chlorine and its compounds
 Bromine (use in swimming pools)
 Iodine (used in tablet form)
 Phenol and phenolic compounds
 Acids and alkalies
 Heavy metals and related compounds
 Dyes
 Soaps and synthetic detergents
 Hydrogen peroxide
 Quaternary ammonium compounds.
CHLORINATION
 Chlorination is the process of adding chlorine to
drinking water to disinfect it and kill germs.
Different processes can be used to achieve safe
levels of chlorine in drinking water
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Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD
CHLORINATION PRACTICS
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD76
Plain or Simple Chlorination:
The application of chlorine to raw water before
releasing for drinking is called as plain chlorination.
 This is use when, turbidity and colour of water is low.
 Row water is less polluted.
 Iron and manganese concentration is less then 0.3
mg/lit
Breakpoint chlorination
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD77
 Breakpoint chlorination is the application of sufficient chlorine to
maintain a free available chlorine residual.
 The addition of chlorine to a water that contains ammonia or nitrogen-
containing organic matter produces an increased
combined chlorine residual.
Water softening methods
Prof.C.P.Thosar@ CSMSS
CSCOE,AURANGABAD78
 Ion-exchange resin method.
 Lime softening.
 Washing soda method.
 Distillation and rain water.
 Reverse osmosis.

Unit 2

  • 1.
    SUBJECT- ENVIRONMENTAL ENGINEERING CSMSSCSCOE,AURANGABAD 1 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 2.
    MODULE - 2 TREATMENTOF WATER 2 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 3.
    CONTENT  CONVEYANCE OFRAW WATER PIPELINES AND CANALS  DESIGNING OF RISING MAINS  TYPE OF VALVES  TYPE OF PUMPS  INTAKE STRUCTURE  TREATMENT OF WATER  AERATION  SEDIMENTATION  COAGULATION  RAPIT MIXING  CLARIFLOCCCULATOR  DESIGN CRITRRIA FOR FLOCCULATION BASIN USING ROTATION PADDLES  PLATE SETTLER 3 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 4.
    CONTENT  TUBE SETTLER FILTRATION  TYPESOF FILTERS  DISINFACTION  REQUIREMENT OF AN IDEAL DISINFACTANT  MECHANISM OF DISINFACTION  WATER SOFTENING METHODS  DEMINERALISATION/DEIONIZATION 4 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 5.
    2.1CONVEYANCE OF RAWWATER PIPELINES AND CANALS  2.1.1.Pipelines  2.2.2.Aqueducts (Open channels)  2.1.3.Advantages of Pipelines and Aqueduct Systems  2.1.4 Disadvantages of Pipelines and Aqueduct Systems  2.1.5 Hydraulics of Conduits 5 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 6.
    2.1.5 Hydraulics ofConduits  Fluid Flows 1.Classification Based on Variation with time 2. Classification Based on Variation with space  Flow Type & Examples A steady flow can be uniform or non-uniform and similarly an unsteady flow can also be uniform or non-uniform. For steady flow discharge is constant with time and for a uniform flow the area of cross section of the fluid flow flow is constant through the flow path. 6 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 7.
    2.1.6 Laying ofPipes 7 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 8.
    2.1.7 Joints inPipes 1.Joints in Cast Iron Pipes (a)Bell and Spigot Joint 8 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 9.
  • 10.
    2.Joints in ConcretePipes (a)Cement Collar Joint (b)Simplex Joint 10 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 11.
    2.1.8.Testing of Pipelines A Pipeline section about 300 m length is tested for leakage, strength etc. 1.Pressure Test 11 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 12.
  • 13.
    2.2DESIGNING OF RISINGMAINS 2.2.1 RISING MAINS The water, after pumped, is taken to the high levelled gravity pipe through the rising main.  The rising main may be of cast iron or asbestos cement pressure pipes.  The velocity of flow in the rising main should not be less then 0.75 m/sec. at any time of flow. 2.2.2 DESIGN STEPS Following are the step for design of the rising main. STEP 1:Assume the velocity of flow in the rising main. STEP 2:Determine required cross-sectional area of the rising main. STEP 3: 2:Determine required diameter of rising main.13 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 14.
    2.3 TYPE OFVALVES  The fixtures which are fixed along the distribution system are know as valves.  PURPOSES SERVED 1.Control the rate of flow of water. 2.Releases or admits air into the pipeline. 3. Prevents or detects leakage. 4.Meets the demand during emergencies. 5.Make the distribution system more efficient. 14 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 15.
  • 16.
    2.3.2 AIR RELIEFVALVE 16 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 17.
  • 18.
    2.4 TYPE OFPUMPS  2.4.1Gear Pumps 18 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 19.
     2.4.2 RotaryVane Pumps  2.4.3Screw Pumps 19 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 20.
     2.4.4 BentAxis Pumps  2.4.5 Inline Axis Pumps 20 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 21.
     2.4.6 RadialPiston Pumps 21 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 22.
    2.5 INTAKE STRUCTURE The raw water required for any water supply scheme is withdrawn from a surface source like river, reservoir, lake or canal, or from underground source like well or spring.  When the withdrawal of water is from surface source, a constriction called intake structure is provided to collect fluctuating levels, and discharge it into pipe.  Intake structure mainly consist of: 1) Conduit with protective works, 2) Screens at open ends 3) Gates and valves to regulate the flow, and 22 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 23.
    2.5.1 FACTORS GOVERNINGTHE LOCATION OF INTAKE  It should be near the treatment plant to cut down the cost of conveyance.  It should be located in the comparatively pure zone of water source to reduce the load on treatment work.  It should not be located on the downstream side of the sewage disposal.  It should not be located on curves.  It should be located at such a site from where it can draw water even during driest period of year.  It should be away from navigation channels as it may admit raw water polluted by discharge of wastes by ships.23 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 24.
    2.5.2 TYPES OFINTAKES  1.SUBMERGED OR LAKE INTAKE  2.EXPOSED INTAKES A) Canal Intake. B) Reservoir Intake.  3.RIVER INTAKE.  4. MOVEBLE INTAKE 24 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    1.SUBMERGED OR LAKEINTAKE 25 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.EXPOSED INTAKES A) CanalIntake. 26 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.6 TREATMENT OFWATER 2.6.1 Necessity of Treatment of Water  The following are the objectives of treatment of water.  To make water odour free and tasty.  To make the water safe and sparkling for drinking and domestic purposes.  To make it colourless.  To remove dissolved gases and turbidity of water.  To make it free from all objectionable impurities present in suspension, colloidal or dissolved from. 30 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 31.
     To removeharmful bacteria.  To remove hardness of water.  To make the water suitable for a wide variety of industrial purposes like dyeing, brewing, soft drinks, steam generation etc. 31 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.6.2.LAYOUT AND COMPONENTS OFWATER TREATMENT PLANT 32 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.7 AERATION  Theprocess of exposing large surface of water to the atmospheric air is called aeration.  Its main purpose is to absorb more oxygen and let out unpleasant odours and gases and oxidise Fe and Mn in water. 34 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 35.
    2.7.1 Objectives ofAeration  To increase oxygen contents in water for imparting freshness.  To expel volatile substances and gases like H2S,CO2,causing bad taste and odour.  To oxidize iron and manganese so that these can be precipitated and removed.  To destroy bacteria to some extent, by agitation of water during aeration. 35 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.7.2 METHODS OF AERATIONS 1.ByUsing Fountains, Spray Nozzles. 36 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.Gravity or FreeFall Aerators. (a)Cascade Aerators: 37 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    3.Trickling Beds orMultiple Trays. 39 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    EXAMPLES  The maximumdaily demand of water is 114 MLD. Design aeration fountain(cascade aerator). Solution: Q=114MLD (i) Diameter of bottommost cascades: Design flow, Q= 114MLD = 114 X 106 Lit/day = 4750 m3/hr. Loading rate= 0.03m2/m3/hr. 41 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.8 SEDIMENTATION  Principleof sedimentation is applied for the removal of (i) Grit in grit chamber (ii) Destabilized floc in clariflocculators, (iii) Particulate matter in primary and secondary settling basins. 44 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
  • 45.
    2.8.1 TYPE OF SEDIMENTATION 1.PLAINSEDIMNETATION (Settling velocity of a discrete particle depends upon specific gravity and diameter of the particle, gravitational acceleration and kinematic viscosity) 2. SEDIMENTATION WITH COAGULATION OR CHEMICALLY ASSISTED SEDIMENTATION 45 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.8.2 Type ofSedimentation Tanks  1.Fill and Draw Type. 46 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.Continuous Flow Tank (a)Horizontal Flow Type: 47 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.9 COAGULATION  Theprocess of mixing certain chemicals to water to neutralize the electrical charges and to form an insoluble, gelatinous flocculent precipitate for absorbing and entraining suspended and colloidal particles of impurities is called coagulation. 49 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    Factor affecting Coagulation Type of coagulant  Dose of coagulant  Time and method of mixing the coagulant.  Character of water 1. Ph of water 2. Temperature of water 3. Nature and quantity of suspended matter. 50 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.9.2. Coagulation process Following processes 1. Feeding 2. Mixing 3. Flocculation 4. Clarification or sedimentation. 51 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    By toothed wheelBy helical screw Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD52 1. Feeding- a)Dry feeding
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    B) Wet feeding Prof.C.P.Thosar@CSMSS CSCOE,AURANGABAD53
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     Mixing In orderto cause the complete dispersion of the added coagulant into the entire mass of water, mixing devices are required. The violent agitation of water can be achieved by using mixing devices like compressed air, centrifugal pumps and mixing basins. 54 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD55  Compressedair device. (By passing compressed air from bottom surface of mixing basin)  Centrifugal pump. (There will be efficient dispersion of coagulant in water while passing through the impeller of pump.)  Mixing channel with flume.
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     Flocculation In colloidchemistry, flocculation refers to the process by which fine particulates are caused to clump together into a floc. The floc may then float to the top of the liquid (creaming), settle to the bottom of the liquid (sedimentation), or be readily filtered from the liquid. 58 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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     Clarification orsedimentation. After flocculation water is admitted into basins called clarifiers or settling basins. Water is detained in a such tank for a detention generated under flocculation, settles down in the form of sludge The clear water taken out through outlet arrangements and generally admitted to filtration tanks for further purification. 60 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.9.4 Common Coagulants Followingcommon coagulants are used: 1. Alum or aluminum sulphate. 2. Chlorinated copperas 3. Magnesium carbonate and lime 4. Ferrous sulphate and lime 5. Sodium aluminate 6. Polyelectrolytes. 63 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.11 CLARIFLOCCULATOR  Clariflocculatoris a combination of flocculation and clarification in a single tank. It has two concentric tanks where inner tank serves as a flocculation basin and the outer tank serves as a clarifier. 64 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.15 FILTRATION  Filtrationis the process of separating suspended solid matter from a liquid, by causing the latter to pass through the pores of some substance, called a filter. The liquid which has passed through the filter is called the filtrate.  Filtration is a process of removing particulate and bacterial impurities which could not be removed in earlier processes, from water by passing it through a porous medium.  It is an important stage in the purification of water. 66 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.15.2 FILTER MATERIALS Sand  Anthracite Anthracite, often referred to as hard coal, is a hard, compact variety of coal that has a sub-metallic luster. It has the highest carbon content, the fewest impurities, and the highest energy density of all types of coal and is the highest ranking of coals. [ Carbon content (%): 92 – 98]  Garnet sand or limonite  Locally available materials  Gravel 67 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.16 TYPE OFFILTERS 2.16.1 SLOW SAND FILTER The filter media is supported by this base material LAYER SIZE OF GRAVEL First layer(Bottom) 40 TO 65 mm Second layer 20 TO 40 mm Third layer 6 TO 20 mm Fourth layer(Topmost) 3 TO 6 mm 68 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.16.2 RAPID SANDFILTER OR MECHANICAL SAND FILTER. 70 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    2.17 DISINFECTION  Disinfectionis a process of killing all pathogens.  Sterilization is a process in which the total and complete destruction of all types of bacteria takes place.  Theory of Disinfection Safe water means 1.Water free from bacteria. 2.Water aesthetically acceptable. 3.Water free from excessive minerals and poisonous matter. 72 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    Factors affecting theefficiency of disinfection. Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD73  Nature and concentration of organisms.  Nature and concentration of disinfectant.  Temperature of water.  Time of contact  Nature of physical agent.  Nature of water to be disinfected.  pH of water.
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    Disinfecting agents. Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD74 1.Physicalagents.  Heat  Light (natural sun radiation, artificial) 2.Chemical agents.  Potassium permanganate (used in hospitals)  Ozone  Chlorine and its compounds  Bromine (use in swimming pools)  Iodine (used in tablet form)  Phenol and phenolic compounds  Acids and alkalies  Heavy metals and related compounds  Dyes  Soaps and synthetic detergents  Hydrogen peroxide  Quaternary ammonium compounds.
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    CHLORINATION  Chlorination isthe process of adding chlorine to drinking water to disinfect it and kill germs. Different processes can be used to achieve safe levels of chlorine in drinking water 75 Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD
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    CHLORINATION PRACTICS Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD76 Plainor Simple Chlorination: The application of chlorine to raw water before releasing for drinking is called as plain chlorination.  This is use when, turbidity and colour of water is low.  Row water is less polluted.  Iron and manganese concentration is less then 0.3 mg/lit
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    Breakpoint chlorination Prof.C.P.Thosar@ CSMSS CSCOE,AURANGABAD77 Breakpoint chlorination is the application of sufficient chlorine to maintain a free available chlorine residual.  The addition of chlorine to a water that contains ammonia or nitrogen- containing organic matter produces an increased combined chlorine residual.
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    Water softening methods Prof.C.P.Thosar@CSMSS CSCOE,AURANGABAD78  Ion-exchange resin method.  Lime softening.  Washing soda method.  Distillation and rain water.  Reverse osmosis.