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10 Pipe Flow Problems Solved Step by Step (Fluid Mechanics)

10 solved pipe flow problems for engineering students: Reynolds number, friction factor, head loss, pump power, NPSH. Complete solutions with formulas.

Pipe Flow Problems for Engineering Students

These 10 problems cover the core calculations in pipe flow hydraulics. Each includes full step-by-step solutions. Perfect for studying fluid mechanics, hydraulic engineering, or preparing for the FE/PE exam.

Problem 1: Reynolds Number

Water at 20°C flows through a 150 mm steel pipe at 3 L/s. Determine the flow regime.

Solution:

A = pi × 0.15² / 4 = 0.01767 m²
V = 0.003 / 0.01767 = 0.170 m/s
Re = V × D / v = 0.170 × 0.15 / (1.004×10⁻⁶)
Re = 25,398 → Turbulent (Re > 4000)

Problem 2: Friction Factor (Swamee-Jain)

For Problem 1, calculate the Darcy friction factor. Steel roughness ε = 0.045 mm.

Solution:

ε/D = 0.000045 / 0.15 = 0.0003
f = 0.25 / [log10(0.0003/3.7 + 5.74/25398^0.9)]²
f = 0.25 / [log10(0.0000811 + 0.000476)]²
f = 0.25 / [-3.253]²
f = 0.0236

Problem 3: Head Loss (Darcy-Weisbach)

Calculate the friction head loss for 200 m of the pipe from Problems 1-2.

Solution:

hf = f × (L/D) × V²/(2g)
hf = 0.0236 × (200/0.15) × 0.170²/(2×9.81)
hf = 0.0236 × 1333.3 × 0.001474
hf = 0.046 m

Very low head loss because the velocity is low (0.17 m/s). This pipe is oversized.

Problem 4: Head Loss (Hazen-Williams)

Repeat Problem 3 using Hazen-Williams. C = 120 for steel.

Solution:

hf = 10.67 × 200 × 0.003^1.852 / (120^1.852 × 0.15^4.87)
hf = 2134 × 1.664×10⁻⁵ / (6932.5 × 6.97×10⁻⁵)
hf = 0.0355 / 0.000483
hf = 0.073 m

Hazen-Williams gives a slightly different result (0.073 m vs 0.046 m). Both are acceptable for this low-velocity case.

Problem 5: Fitting Losses

A pipe section has 3 standard 90° elbows, 1 gate valve (open), and 1 check valve. V = 2.0 m/s. Calculate total fitting losses.

Solution:

K = 3×0.30 + 0.20 + 2.50 = 3.60
hm = 3.60 × 2.0²/(2×9.81)
hm = 3.60 × 0.2039
hm = 0.73 m

Problem 6: Total Dynamic Head (TDH)

A pump must deliver 5 L/s from a ground-level cistern to a tank 20 m above. Piping: 50 m of 3" PVC (C=150). Fittings: K_total = 6.5. Calculate TDH.

Solution:

Static head: Hg = 20 m

Friction (H-W):
D = 0.0762 m, Q = 0.005 m³/s
hf = 10.67 × 50 × 0.005^1.852 / (150^1.852 × 0.0762^4.87)
hf = 1.24 m

Velocity: V = 0.005/0.00456 = 1.10 m/s
Fittings: hm = 6.5 × 1.10²/(2×9.81) = 0.40 m

TDH = 20 + 1.24 + 0.40 = 21.64 m
With 15% safety: TDH = 24.9 m

Problem 7: Pump Power (WHP and BHP)

For Problem 6, calculate the required pump power. Pump efficiency = 65%.

Solution:

WHP = Q × TDH / 76 = 5 × 24.9 / 76 = 1.64 HP
BHP = WHP / η = 1.64 / 0.65 = 2.52 HP
Select motor: 3 HP (next standard size)

Problem 8: NPSH Available

Pump is 3 m above the water surface. Suction pipe: 4 m of 3" PVC with foot valve (K=2.5) and 1 elbow (K=0.3). Water at 25°C, sea level. Calculate NPSHa.

Solution:

Pa/(ρg) = 10.34 m
Pv/(ρg) = 0.324 m (at 25°C)
Hs = -3 m (pump above water)

Suction velocity = 1.10 m/s
hf_suction = 0.10 m (4 m PVC friction)
hm_suction = (2.5 + 0.3) × 1.10²/(2×9.81) = 0.17 m

NPSHa = 10.34 - 0.324 - 3 - 0.10 - 0.17 = 6.75 m

If pump NPSHr = 3.0 m → margin = 3.75 m ✅ Safe.

Problem 9: Optimal Pipe Diameter

Find the optimal discharge pipe diameter for 10 L/s at recommended velocity 1.5 m/s.

Solution:

D = sqrt(4Q / (π×V))
D = sqrt(4×0.010 / (π×1.5))
D = sqrt(0.00849)
D = 0.092 m = 92 mm

Select next commercial size: 100 mm (4"). Check velocity: V = 0.010/0.00785 = 1.27 m/s ✅ Within range.

Problem 10: Water Hammer Pressure Surge

Steel pipe 300 m long, velocity 2.0 m/s. Valve closes instantly. Wave speed c = 1100 m/s. Calculate pressure surge and critical closing time.

Solution:

Pressure surge:
ΔH = c × ΔV / g = 1100 × 2.0 / 9.81 = 224.3 m

Critical closing time:
tc = 2L / c = 2 × 300 / 1100 = 0.545 s

224 m of water hammer! Close the valve in at least 5 × tc = 2.7 seconds to reduce the surge.

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