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Chapter 2 of 9

Water Supply & Treatment

In the UPSC ESE Civil syllabus under Environmental Engineering · 2 parts

📑 Contents (16 sections)

Part 1 of 2

Sources of Water & Intake Structures

Last reviewed 16 Sept 2026 · 7 min read

Sources of water

Water sources are broadly surface or subsurface (groundwater) sources.

Surface sources

Source Quantity Quality
Rivers and streams Large in perennial rivers; flows fluctuate — minimum (lean season) flow governs reliability Turbid in floods; exposed to pollution from towns and industries upstream; needs full treatment
Natural lakes and ponds Depends on catchment and storage; usually reliable for small towns Less turbidity (settling), but algae, tastes and odours; eutrophication risk
Impounding reservoirs (dams) Large, regulated supply — stores monsoon flows for dry seasons Clearer water due to settling; stratification in deep reservoirs; algae; quality varies with depth (so multi-level intakes)
Canals Depends on canal operation (closures) Similar to river water, with contamination risk along the route

Subsurface sources

Source Features
Springs Natural outflow of groundwater; gravity springs (water table cuts the ground surface), surface springs, artesian springs; supply for hill towns
Infiltration galleries Horizontal perforated conduits laid in sand/gravel along or under river beds; collect naturally filtered water
Infiltration wells Shallow wells sunk in river beds, connected to a jack well
Open (dug) wells Shallow unconfined aquifers; small supplies
Tube wells Deep aquifers; large yields; common source for towns and rural schemes

Groundwater is generally clear, free of pathogens and cooler, but may be hard or contain iron, fluoride, arsenic, nitrate or salinity; quantity is limited by aquifer recharge.

Alternative sources

  • Rainwater harvesting — rooftop and surface runoff collection for storage or recharge.
  • Desalination of sea or brackish water (reverse osmosis, multi-stage flash distillation) — energy-intensive; used in some coastal cities.
  • Reuse of treated wastewater for non-potable uses (industry, gardening, flushing).

Selection of a source

  1. Quantity — adequate for the design period, including in droughts.
  2. Quality — minimum treatment required; free from pollution risk.
  3. Distance and elevation — nearer and higher sources reduce conveyance and pumping cost (gravity supply preferred).
  4. Cost — capital and operation and maintenance.
  5. Reliability and legal rights — water rights, inter-state issues.

Intake structures

An intake is a structure placed in or near a source to withdraw water and discharge it into the conveyance system (intake conduit, jack well, pumping main). It is usually a masonry or concrete structure with openings fitted with screens.

Types

Type Description
River intake Circular masonry tower (intake well) in or near the river with ports at different levels; water flows through screens into the well and is pumped out
Reservoir intake Tower near the dam (often part of it) with inlets at several levels so the best-quality water can be drawn as the level changes; access by a foot bridge
Lake intake Pipe or conduit laid in the lake bed with a bell-mouth entry protected by a crib or screen; conveys water to a shore sump
Canal intake Masonry chamber on the canal bank with a screened inlet pipe
Submerged intake Entirely under water (a crib of timber/concrete with pipe entry); cheap, does not obstruct navigation, but hard to inspect and clean
Exposed intake Tower above water level; accessible for maintenance and operation of gates
Wet intake tower Water enters the tower well (water level inside ≈ source level) and then flows into the conduit through gates
Dry intake tower Inlet pipes lead directly to the conduit; the tower is dry inside; water can be drawn from any level independently; tower must be designed for buoyancy/uplift

Site selection for intakes

  1. Located upstream of towns and sewage or industrial outfalls, where water is purest.
  2. Adequate depth of water at the lowest level (entry below the lowest water level) — preferably on a straight stable reach or the concave (deep) side of a bend.
  3. Good foundations and safety against scour, floods, floating debris and ice.
  4. Not in navigation channels; easy access.
  5. Should not be where heavy currents or rapids cause damage; avoid sites with sand bars forming.
  6. Close to the treatment plant and supply area where possible, and able to accommodate future expansion.

Design considerations

  • Screens: coarse screens (bars) at the entry to exclude large floating matter, and fine screens for smaller debris; cleaned manually or mechanically.
  • Low entrance velocity through the ports (commonly well below about 0.6 m/s) to avoid drawing in debris, sediment and fish.
  • Inlets at multiple levels (reservoir and river intakes) — withdraw clearer water as levels and quality vary.
  • Stability against water pressure, wave and ice forces, buoyancy (dry towers), scour.
  • Capacity for the maximum daily demand at the end of the design period (intake structures commonly designed for about 30 years).
  • Provision for isolation (gates/valves) and cleaning.

Conveyance of raw water

  • Gravity (free-flow) conduits — canals, aqueducts, flumes, tunnels, grade aqueducts; follow the hydraulic gradient; cheap where terrain permits.
  • Pressure conduits — pipelines (mild steel, ductile iron, prestressed concrete, GRP, HDPE) that can follow ground undulations below the hydraulic gradient line.
  • Pumping from a jack well/sump at the intake through a rising main to the treatment plant; pumps designed for maximum daily flow with standby units.
FormulaPumping power

= total head = static lift + friction and minor losses; = overall efficiency of the pump set.

Economical diameter of a rising main is found by balancing pipe capital cost (increases with diameter) and pumping energy cost (decreases with diameter); velocities of roughly 1–2 m/s are commonly economical.

Part 2 of 2

Water Treatment

Last reviewed 16 Sept 2026 · 13 min read

Treatment flow sheet

A conventional surface water treatment plant:

Intake and screens → (plain sedimentation for very turbid water) → aeration (if needed) → rapid mixing with coagulant → flocculation → sedimentation (clarification) → rapid sand filtration → disinfection → clear water reservoir → distribution

Groundwater often needs only aeration, iron/manganese removal and disinfection; hard or fluoride-rich water needs special treatment.

Unit Main impurity removed
Screening Large floating matter
Aeration Dissolved gases (CO₂, H₂S), tastes and odours; oxidises iron and manganese
Plain sedimentation Settleable suspended solids
Coagulation–flocculation–sedimentation Colloidal turbidity and colour
Filtration Remaining fine flocs, turbidity, some bacteria
Disinfection Pathogens
Softening Hardness

Screening

  • Coarse screens (bar racks) at the intake to exclude floating debris, and fine screens or micro-strainers for smaller matter and algae.
  • Cleaned manually or mechanically; velocity through screens kept low.

Aeration

Brings water into intimate contact with air:

  • Removes CO₂ (reduces corrosiveness), H₂S and volatile tastes and odours.
  • Adds oxygen — oxidises dissolved iron and manganese to insoluble forms that can be settled and filtered.

Types: spray aerators (nozzles), cascade aerators (water flows down steps), multiple tray aerators (perforated trays with coke/gravel), diffused air aerators (compressed air bubbled through water), mechanical aerators.

Sedimentation

Types of settling

Type Description Example
Type I — discrete settling Particles settle individually without interaction at constant velocity Plain sedimentation of sand/silt, grit chambers
Type II — flocculent settling Particles coalesce, grow and settle faster Coagulated water, primary sewage settling
Type III — zone (hindered) settling High concentration; particles settle as a mass with a distinct interface Secondary clarifiers (activated sludge)
Type IV — compression Particles form a structure compressed by the weight above Sludge thickeners, bottom of clarifiers
FormulaDiscrete settling

Stokes' law (laminar, , small particles):

Ideal settling basin (Camp–Hazen):

  • Surface overflow rate (SOR) (m³/m²/day) — equal to the settling velocity of the smallest particle removed completely.
  • Particles with are removed 100%; particles with are removed in the fraction .
  • Removal depends on surface area, not on depth (in theory).

Detention time ; horizontal velocity (kept below the scour velocity); weir loading = ÷ weir length.

Typical design values (clarifiers after coagulation, CPHEEO guidance): detention time about 2–2.5 h; surface loading about 30–40 m³/m²/day; weir loading not exceeding about 300 m³/m/day. Plain sedimentation tanks without coagulant need longer detention.

Types of tanks

  • Horizontal-flow rectangular tanks — long, narrow; inlet and outlet baffles; sludge scraped to a hopper.
  • Circular radial-flow tanks — central feed, peripheral weir; rotating scraper.
  • Upflow (hopper-bottom) tanks and sludge blanket clarifiers.
  • Tube (lamella) settlers — inclined tubes or plates reduce the settling distance, greatly increasing capacity in a small area.

Coagulation and flocculation

Colloidal particles (clay, colour, bacteria) are negatively charged and repel each other, so they do not settle. Coagulation destabilises them; flocculation gently brings them together into large, settleable flocs.

Mechanisms

  1. Charge neutralisation — positively charged hydrolysis products of coagulants neutralise particle charges.
  2. Double-layer compression.
  3. Sweep (enmeshment) coagulation — particles trapped in precipitating metal hydroxide flocs (dominant at usual alum doses).
  4. Inter-particle bridging — by long-chain polymers.

Coagulants

Coagulant Features
Alum — aluminium sulphate Most common; cheap; best pH about 6.5–8.5; consumes alkalinity
Ferrous sulphate (copperas) + lime For high pH waters; used where lime is added anyway
Chlorinated copperas (ferric sulphate + ferric chloride) Effective over a wide pH range; removes colour
Ferric chloride / ferric sulphate Wide pH range, dense flocs; corrosive
Sodium aluminate For waters low in alkalinity; also used in softening
Poly-aluminium chloride (PAC) Pre-hydrolysed; effective at low doses and low temperatures; less alkalinity consumed

Coagulant aids: activated silica, bentonite clay, polyelectrolytes (cationic, anionic, non-ionic polymers), lime or soda ash (to supply alkalinity or adjust pH).

Alum reaction with natural alkalinity:

1 mg/L of commercial alum (, molecular weight ≈ 666) consumes about 0.45 mg/L alkalinity as CaCO₃.

Jar test — samples dosed with different coagulant amounts are rapidly mixed, flocculated and settled in a gang stirrer; the dose giving the best clarity at least cost is the optimum dose.

Mixing and flocculation

FormulaVelocity gradient (Camp and Stein)

= power input (W); = dynamic viscosity; = volume of the tank.

Paddle flocculator: , where = relative velocity of paddles with respect to water (≈ 0.75 × paddle tip velocity).

The dimensionless product measures the opportunity for particle collisions.

  • Rapid (flash) mixing — intense agitation for a few seconds to about a minute (high ) to disperse coagulant uniformly: mechanical flash mixers, hydraulic jumps, baffles, in-line mixers.
  • Flocculation (slow mixing) — gentle agitation for about 10–40 minutes with low (commonly about 10–75 s⁻¹) so flocs grow without breaking: paddle flocculators, baffled channels.
  • Clariflocculator — a circular unit combining a central flocculation zone with an outer clarifier; widely used in India.

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