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Hydraulic Design — Pipe Sizing

Sizing process pipework by Darcy–Weisbach friction loss and velocity limits: continuity, Reynolds number, Colebrook/Swamee–Jain friction factor, self-scour velocity bands and a worked diameter comparison.

0.9–2.4
m/s band
Darcy
–Weisbach
v∝1/D²
scaling

Sizing Pipework by Friction & Velocity

Pipe diameter is the first hydraulic decision and it cascades into everything else — pump head, energy cost, water hammer, solids deposition and capital cost. Size a line too small and friction loss and erosion soar; too large and solids settle, capital is wasted and self-cleansing velocity is never reached. The right diameter falls out of two constraints handled together: a friction-loss budget (Darcy–Weisbach) and a velocity band.

Darcy–Weisbach, Reynolds & Colebrook

Continuity fixes velocity once a diameter is chosen:

ContinuityQ = A · v = (πD²/4) · v

Friction head loss along a full-flowing pipe follows Darcy–Weisbach:

Darcy–Weisbach friction losshf = f · (L/D) · (v² / 2g)

The friction factor depends on the Reynolds number and relative roughness; for turbulent flow it is given implicitly by Colebrook–White, or explicitly by the Swamee–Jain approximation:

Reynolds numberRe = ρvD/μ = vD/ν
Swamee–Jain friction factor (turbulent)f = 0.25 / [ log10( ε/3.7D + 5.74/Re0.9 ) ]²

Fast Enough to Scour, Slow Enough to Control

ServiceTypical velocity (m/s)Why
Pump suction0.6–1.5Low loss protects NPSH and avoids cavitation
Pump discharge / process1.0–2.4Self-scouring without excess friction or hammer
Sludge / solids-bearing1.2–2.0Above the deposition (settling) velocity
Gravity sewer / drain≥0.7 (self-cleansing)Prevents grit and solids accumulation
Long transfer mains0.9–1.5Low velocity caps pumping energy and surge

Velocity scales with the inverse square of diameter at fixed flow (v ∝ 1/D²), and friction loss roughly with v² — so a one-size increase can cut head loss dramatically while pushing velocity toward the deposition limit. The art is landing inside the band at the diameter that minimises lifetime cost (capital + pumping energy).

Sizing a Transfer Main

Worked example: DN150 vs DN200 for 40 L/s

Transfer Q = 40 L/s = 0.040 m³/s of water at 20°C through 250 m of steel pipe (ε = 0.05 mm).

DN150 (D=0.1541 m): v = 0.040 / (π·0.1541²/4) = 2.14 m/s  ·  Re ≈ 3.3×105
DN200 (D=0.2027 m): v = 0.040 / (π·0.2027²/4) = 1.24 m/s  ·  Re ≈ 2.5×105
hf,DN150 ≈ f(L/D)(v²/2g) ≈ 0.018×(250/0.1541)×(2.14²/19.62) ≈ 6.8 m
DN200 drops friction loss to ≈ 1.6 m — about 4× less head for ~75% more pipe cost. Both sit in-band; DN200 is usually justified on a long main by the pumping-energy saving. Confirm with the pressure-drop calculator and a lifecycle comparison.

Run the Numbers

Size the diameter and check head loss and erosional velocity with the pipe hydraulics tools.

Related Hydraulic Design

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