8.5 Water Supply: Demand, Storage, Pumping, Distribution, and Treatment

Key Takeaways

  • Design demand is population × per capita consumption, scaled by peak factors for the maximum day and peak hour.

  • Distribution storage combines equalizing storage, fire reserve and emergency reserve.

  • Pump water power is γQH, and brake power is γQH divided by pump efficiency.

  • A settling basin removes particles whose settling velocity exceeds the overflow rate Q/A, independent of tank depth.

  • Geometric population growth projects P = P₀(1 + r)ⁿ, while arithmetic growth adds a constant number per year.

Last updated: October 2026

8.5 Water Supply: Demand, Storage, Pumping, Distribution, and Treatment

The 2022 HGE table of specifications gives Water Supply 8% of the subject, or 4 of its 50 items. That is as much as buoyancy and flotation, and more than hydrodynamics. The items are computational and draw directly on pipe flow (Section 8.3) and on pumps and the energy equation (Section 8.1).


Population Forecasting

MethodFormulaUse
ArithmeticPn=P0+n kaP_n = P_0 + n\,k_aMature towns with steady growth
Geometric (uniform percentage)Pn=P0(1+r)nP_n = P_0(1 + r)^nYoung, growing towns
Exponential (continuous)Pn=P0eknP_n = P_0 e^{kn}Equivalent to geometric growth with continuous compounding
Declining growth rateGrowth slows as the population approaches a saturation valueLarge cities

Example. A town of 40,000 grew 3% per year. Projected to a 20-year design period: P=40,000(1.03)20=72,244P = 40{,}000(1.03)^{20} = 72{,}244. An arithmetic increase of 1,200 per year would give 40,000+20(1,200)=64,00040{,}000 + 20(1{,}200) = 64{,}000.


Water Demand and Peaking Factors

Average day demand (ADD):

ADD=P×q(liters per capita per day)\text{ADD} = P \times q \quad \text{(liters per capita per day)}

Here qq includes domestic use, commercial and institutional use, and an allowance for non-revenue water (leakage).

Demand conditionTypical peaking factorUsed for
Maximum day demand (MDD)about 1.2 to 1.5 × ADDSource, treatment plant and transmission main capacity
Peak hour demand (PHD)about 1.5 to 3.0 × ADDDistribution network sizing
Fire demandFire flow for a set duration, added to MDDDistribution mains, hydrants, fire reserve

Smaller communities have higher peak factors, because their demand is less spread out over time.

Example. A population of 72,000 uses 150 L/capita/day.

  • ADD =72,000×150=10.8×106 L/day=10,800 m3/day=0.125 m3/s= 72{,}000 \times 150 = 10.8 \times 10^6\text{ L/day} = 10{,}800\text{ m}^3/\text{day} = 0.125\text{ m}^3/\text{s}.
  • With MDD = 1.3 × ADD, MDD =0.1625 m3/s= 0.1625\text{ m}^3/\text{s}.
  • With PHD = 2.0 × ADD, PHD =0.250 m3/s= 0.250\text{ m}^3/\text{s}.

Storage

Elevated tanks and ground reservoirs hold three volumes:

  1. Equalizing (operational) storage covers hourly demand above the steady supply rate. It is found from a mass diagram: plot cumulative supply and cumulative demand over a day. The required storage is the largest surplus plus the largest deficit, measured from the supply line. Rule-of-thumb values are often around 15% to 25% of MDD.
  2. Fire reserve equals fire flow times fire duration.
  3. Emergency reserve covers power or source outages.

Example. A pumping plant delivers a steady 500 m3/h500\text{ m}^3/\text{h} for 24 hours. Cumulative demand exceeds cumulative supply by at most 1,100 m31{,}100\text{ m}^3 at 8 PM, and falls below it by at most 900 m3900\text{ m}^3 at 5 AM. Equalizing storage is 1,100+900=2,000 m31{,}100 + 900 = 2{,}000\text{ m}^3.

Pressure. An elevated tank's water surface sets the hydraulic grade line. Residual pressure at a service point is the HGL elevation minus ground elevation, less head losses. Distribution systems typically aim to keep enough residual pressure for upper-floor fixtures without excessive pressure that drives leakage.


Pumping

Pwater=γQH,Pbrake=γQHηp,Pmotor input=γQHηpηmP_{\text{water}} = \gamma Q H, \qquad P_{\text{brake}} = \frac{\gamma Q H}{\eta_p}, \qquad P_{\text{motor input}} = \frac{\gamma Q H}{\eta_p \eta_m}

Total dynamic head is H=(static lift)+(friction losses)+(minor losses)+(velocity head at discharge, if free)H = (\text{static lift}) + (\text{friction losses}) + (\text{minor losses}) + (\text{velocity head at discharge, if free}).

Example. A pump delivers 0.08 m3/s0.08\text{ m}^3/\text{s} from a well with its water level at elevation 12 m to a tank surface at elevation 52 m. Pipe losses total 6 m, and the pump efficiency is 0.75.

  • H=40+6=46 mH = 40 + 6 = 46\text{ m}.
  • Brake power =9.81(0.08)(46)/0.75=48.1 kW= 9.81(0.08)(46)/0.75 = 48.1\text{ kW}.

Cavitation. The available net positive suction head must exceed the pump's required NPSH, so suction lifts are kept short.


Distribution Systems

Layouts:

  • Branching (tree) systems are simple, but they have dead ends with stagnant water and a single supply path.
  • Grid or loop systems give two-way flow, better pressure and reliability, and are analyzed by the Hardy Cross method (Section 8.3).

Pipe sizing. Choose a diameter so the friction slope keeps pressures acceptable and velocities moderate, roughly 0.6 to 2 m/s. With Hazen-Williams:

hf=10.67 L Q1.852C1.852D4.87h_f = \frac{10.67\, L\, Q^{1.852}}{C^{1.852} D^{4.87}}

Example. A 1,500 m1{,}500\text{ m} main carries the peak-hour flow of 0.25 m3/s0.25\text{ m}^3/\text{s}, and the allowable head loss is 12 m with C=130C = 130. Solving for D:

D4.87=10.67(1,500)(0.25)1.8521301.852(12)=16,005(0.07651)8,186(12)=0.01247D^{4.87} = \frac{10.67(1{,}500)(0.25)^{1.852}}{130^{1.852}(12)} = \frac{16{,}005(0.07651)}{8{,}186(12)} = 0.01247

So D=0.012471/4.87=0.406 mD = 0.01247^{1/4.87} = 0.406\text{ m}. Select the next standard size, 450 mm.


Treatment Hydraulics

ProcessDesign relation
Plain sedimentationOverflow (surface loading) rate vo=Q/Asurfacev_o = Q/A_{\text{surface}}. Particles with settling velocity vs≥vov_s \ge v_o are fully removed, and smaller ones are removed in the ratio vs/vov_s/v_o. Detention time t=V/Qt = V/Q.
Stokes' law for discrete particlesvs=g(ρs−ρw)d218μv_s = \dfrac{g(\rho_s - \rho_w)d^2}{18\mu}
Coagulation and flocculationChemicals such as alum destabilize fine particles, and slow mixing builds flocs that settle
FiltrationRapid sand filters run at roughly 55 to 15 m/h15\text{ m/h} and are cleaned by backwashing; slow sand filters run far slower and rely on a biological layer
DisinfectionChlorination; effectiveness depends on concentration × contact time (CT)

Drinking-water quality limits in the Philippines are set by the Department of Health's Philippine National Standards for Drinking Water.

Example. A rectangular settling tank treats 0.20 m3/s0.20\text{ m}^3/\text{s} at an overflow rate of 30 m3/m2/day30\text{ m}^3/\text{m}^2/\text{day}.

  • Surface area: A=0.20(86,400)/30=576 m2A = 0.20(86{,}400)/30 = 576\text{ m}^2.
  • With a depth of 3.5 m, detention time is 576(3.5)/0.20=10,080 s=2.8 h576(3.5)/0.20 = 10{,}080\text{ s} = 2.8\text{ h}.
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Water Supply System Components
Test Your Knowledge

A town of 25,000 is projected to grow geometrically at 2.5% per year. What is its population after 20 years?

A

40,965

B

43,859

C

37,500

D

38,750

Test Your Knowledge

A settling tank must treat 0.10 m³/s at an overflow rate of 24 m³/m²/day. What surface area is required?

A

240 m²

B

600 m²

C

360 m²

D

420 m²

Test Your Knowledge

A pump lifts 0.05 m³/s through a total dynamic head of 40 m. If the pump efficiency is 0.80, what brake power is required?

A

24.5 kW

B

19.6 kW

C

31.4 kW

D

15.7 kW

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