Hydraulic Engineering: cram pack

Formula sheets, the key method steps for every topic and 10 practice problems, with full solutions at the back.

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1Formulas and methods

Hydrostatic force

Pressure at depth
p = ρgh
Force on a vertical wall
F = ρg·hc·A
Centre of pressure
yp = yc + Ic/(ycA)
Rectangle
Ic = bH³/12

Continuity & Bernoulli

Continuity
A1v1 = A2v2
Bernoulli
p1 + ½ρv1² + ρgz1 = p2 + ½ρv2² + ρgz2
Flow rate
Q = A·v
Circle area
A = πd²/4

Pipe friction & head loss

Reynolds number
Re = V·D/ν = ρ·V·D/μ
Flow regime
laminar below Re ≈ 2000, turbulent above Re ≈ 4000
Mean velocity
V = Q/A, A = π·D²/4
Darcy–Weisbach
hf = f·(L/D)·V²/(2g)
Minor losses
hm = ΣK·V²/(2g)
Typical K values
entrance 0.5, exit 1.0, 90° bend ≈ 0.3
Pressure drop
Δp = ρ·g·hf
Two open reservoirs
Δz = (f·L/D + ΣK)·V²/(2g)
Free outlet
H = (1 + f·L/D + ΣK)·V²/(2g)

Pumps & pump power

Hydraulic power
Ph = ρ·g·Q·H = Q·Δp
Shaft power
Pshaft = Ph/ηpump
Electrical power
Pel = Pshaft/ηmotor
Pump head
H = Δz + Δp/(ρ·g) + hL
System losses
hL = (f·L/D + ΣK)·V²/(2g)

Open-channel flow (Manning)

Manning equation
V = (1/n)·R2/3·S1/2
Flow rate
Q = A·V
Hydraulic radius
R = A/P (P = wetted perimeter, free surface excluded)
Rectangle
A = b·y, P = b + 2y
Trapezoid (side slope z:1)
A = (b + z·y)·y, P = b + 2y·√(1 + z²)
Circular pipe, full or half full
R = D/4
Required slope
S = (n·Q/(A·R2/3))²

2Practice problems

1.Hydrostatic forceMedium
gated = 0.5 mH = 1.5 m

A vertical rectangular gate 1.5 m wide sits in the wall of a tank of water, with its top edge 0.5 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 0.5 mH = 1.5 mb = 1.5 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 1.5 mH = 1.5 m

A vertical rectangular gate 1 m wide sits in the wall of a tank of water, with its top edge 1.5 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 1.5 mH = 1.5 mb = 1 mρ = 1000 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
12d1​ = 150 mm, p1​ = ?d2​ = 100 mm, p2​ = 260 kPa

Water flows at 38 L/s through a horizontal pipe that narrows from 150 mm to 100 mm. The pressure in the narrow section is 260 kPa. Ignoring losses, find the pressure p1 in the wide section.

Q = 38 L/sd1 = 150 mmd2 = 100 mmp2 = 260 kPaρ = 1000 kg/m³
p1 = kPa
4.Continuity & BernoulliHard
12d1​ = 100 mm, p1​ = 140 kPad2​ = 75 mm, p2​ = ?Δz = 2 m

Water flows up through a pipe that narrows from 100 mm to 75 mm while rising 2 m. At section 1 the pressure is 140 kPa and the velocity is 2 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 100 mmd2 = 75 mmp1 = 140 kPav1 = 2 m/sΔz = 2 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
V = 1.8 m/sD = 300 mmL = 300 mf = 0.028

Water (ρ = 1000 kg/m³) flows at 1.8 m/s through a horizontal pipe, 300 m long, with an inside diameter of 300 mm. Use the Darcy friction factor f = 0.028 and g = 9.81 m/s². Find the pressure drop Δp over the pipe in kPa.

V = 1.8 m/sL = 300 mD = 300 mmf = 0.028ρ = 1000 kg/m³
Δp = kPa
6.Pipe friction & head lossHard
K = 5free outletH = ?L = 150 m, D = 250 mm, f = 0.0153× bend (K = 0.3)

A pipe 150 m long with an inside diameter of 250 mm (Darcy friction factor f = 0.015) runs from an open reservoir and discharges as a free jet into the air. The minor losses are a square-edged entrance (K = 0.5), 3 bends (K = 0.3 each) and a valve (K = 5). Use g = 9.81 m/s². How far H must the reservoir surface be above the pipe outlet for a flow rate of 50 L/s?

Q = 50 L/sL = 150 mD = 250 mmf = 0.015Kentrance = 0.5Kbend = 0.3 (×3)Kvalve = 5
H = m
7.Pumps & pump powerMedium
PQ = 150 L/sH = 26 m

A pump delivers 150 L/s of water (ρ = 1000 kg/m³) against a head of 26 m. The pump efficiency is 65% and the electric motor driving it has an efficiency of 95%. Use g = 9.81 m/s². Find the electrical power Pel the motor draws, in kW.

Q = 150 L/sH = 26 mηpump = 65%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 80 L/sΔz = 17 mL = 400 m, D = 200 mm, f = 0.018, ΣK = 6

A pump moves 80 L/s of water (ρ = 1000 kg/m³) from an open lower reservoir to an upper tank whose water surface is 17 m higher. The pipe is 400 m long with an inside diameter of 200 mm and a Darcy friction factor f = 0.018; the minor-loss coefficients add up to ΣK = 6 (entrance and exit included). Use g = 9.81 m/s². Find the head H the pump must add.

Q = 80 L/sΔz = 17 mL = 400 mD = 200 mmf = 0.018ΣK = 6
H = m
9.Open-channel flow (Manning)Medium
b = 3 my = 0.5 m1.5 : 1n = 0.03, S = 0.0008

A trapezoidal grass-lined earth channel has a bottom width of 3 m and side slopes of 1.5:1 (horizontal:vertical). Water flows uniformly 0.5 m deep. Manning n = 0.03 and the bed slope is S = 0.0008. Find the flow rate Q in m³/s.

b = 3 my = 0.5 mz = 1.5n = 0.03S = 0.0008
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 6 my = 1.7 m3 : 1n = 0.025, Q = 58 m³/s

A trapezoidal gravel channel with a bottom width of 6 m and side slopes of 3:1 (horizontal:vertical) must carry 58 m³/s in uniform flow at a depth of 1.7 m. Manning n = 0.025. Find the required bed slope S (in m/m).

Q = 58 m³/sb = 6 my = 1.7 mz = 3n = 0.025
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 27.59 kN

Hydrostatic force on a plane surface: F = ρ·g·yc·A. It acts at the centre of pressure, ycp = yc + Ic/(ycA), which always lies below the centroid.

Centroid depth and area

yc = d + H/2 = 0.5 + 1.5/2 = 1.25 m
A = H·b = 1.5·1.5 = 2.25 m²
gated = 0.5 mH = 1.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·1.25·2.25 = 27.59 kN

Answer

F = 27.59 kN
2.Hydrostatic force

Answer: ycp = 2.333 m

Hydrostatic force on a plane surface: F = ρ·g·yc·A. It acts at the centre of pressure, ycp = yc + Ic/(ycA), which always lies below the centroid.

Centroid depth and area

yc = d + H/2 = 1.5 + 1.5/2 = 2.25 m
A = H·b = 1.5·1 = 1.5 m²
gated = 1.5 mH = 1.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·2.25·1.5 = 33.11 kN

Centre of pressure

Pressure grows with depth, so the resultant acts below the centroid.

Ic = b·H³/12 = 1·1.5³/12 = 0.2813 m⁴
ycp = yc + Ic/(yc·A) = 2.25 + 0.2813/(2.25·1.5) = 2.333 m

Answer

ycp = 2.333 m
3.Continuity & Bernoulli

Answer: p1 = 269.4 kPa

Continuity and Bernoulli: for an incompressible fluid the flow rate is the same at every section, Q = A₁v₁ = A₂v₂. Along a streamline without losses, p + ½ρv² + ρgz is constant, so where the fluid is faster or higher its pressure is lower.

Velocities

v1 = Q/A1 = 0.038/0.01767 = 2.15 m/s
v2 = Q/A2 = 0.038/0.007854 = 4.838 m/s

Bernoulli

p1 = p2 + ½ρ(v2² − v1²) = 260 + ½·1000·(4.838² − 2.15²)/1000 = 260 + 9.393 = 269.4 kPa

Answer

p1 = 269.4 kPa
4.Continuity & Bernoulli

Answer: p2 = 116.1 kPa

Continuity and Bernoulli: for an incompressible fluid the flow rate is the same at every section, Q = A₁v₁ = A₂v₂. Along a streamline without losses, p + ½ρv² + ρgz is constant, so where the fluid is faster or higher its pressure is lower.

Continuity and Bernoulli

Work in Pa, then divide by 1000 to get kPa.

v2 = v1·(d1/d2)² = 2·(100/75)² = 3.556 m/s
½ρ(v1² − v2²) = ½·1000·(2² − 3.556²)/1000 = −4.321 kPa
ρgΔz = 1000·9.81·2/1000 = 19.62 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 140 + (−4.321) − 19.62 = 116.1 kPa

Answer

p2 = 116.1 kPa
5.Pipe friction & head loss

Answer: Δp = 45.36 kPa

Pipe flow: the Reynolds number Re = V·D/ν = ρ·V·D/μ tells laminar flow (Re below about 2000) from turbulent flow (above about 4000). Friction along a pipe costs the Darcy–Weisbach head loss hf = f·(L/D)·V²/(2g). Fittings, valves, the entrance and the exit add minor losses hm = ΣK·V²/(2g). Between two open reservoir surfaces the energy equation gives Δz = hf + hm, with the exit loss K = 1 included.

Head loss

hf = f·(L/D)·V²/(2g) = 0.028·(300/0.3)·1.8²/(2·9.81) = 4.624 m

Pressure drop

The pipe is horizontal and the velocity does not change, so the energy equation reduces to Δp = ρ·g·hf.

Δp = ρ·g·hf = 1000·9.81·4.624 = 45360 Pa = 45.36 kPa

Answer

Δp = 45.36 kPa
6.Pipe friction & head loss

Answer: H = 0.8673 m

Pipe flow: the Reynolds number Re = V·D/ν = ρ·V·D/μ tells laminar flow (Re below about 2000) from turbulent flow (above about 4000). Friction along a pipe costs the Darcy–Weisbach head loss hf = f·(L/D)·V²/(2g). Fittings, valves, the entrance and the exit add minor losses hm = ΣK·V²/(2g). Between two open reservoir surfaces the energy equation gives Δz = hf + hm, with the exit loss K = 1 included.

Velocity

V = Q/A = 0.05/0.04909 = 1.019 m/s
V²/(2g) = 0.05288 m

Loss coefficients

f·L/D = 0.015·150/0.25 = 9
ΣK = 0.5 + 3·0.3 + 5 = 6.4

Energy equation

The outlet jet still carries its velocity head; it is not a loss but it has to be supplied.

H = (1 + 9 + 6.4)·0.05288 = 0.8673 m

Answer

H = 0.8673 m
7.Pumps & pump power

Answer: Pel = 61.96 kW

Pump power: the power given to the water is the hydraulic power Ph = ρ·g·Q·H = Q·Δp. The shaft must deliver more because the pump loses some: Pshaft = Ph/ηpump, and the motor draws Pel = Pshaft/ηmotor. The pump head H follows from the energy equation: static lift + pressure head + all friction and minor losses.

Hydraulic power

Ph = ρ·g·Q·H = 1000·9.81·0.15·26 = 38.26 kW

Shaft power

Pshaft = 38.26/0.65 = 58.86 kW

Electrical power

Pel = 58.86/0.95 = 61.96 kW

Answer

Pel = 61.96 kW
8.Pumps & pump power

Answer: H = 30.88 m

Pump power: the power given to the water is the hydraulic power Ph = ρ·g·Q·H = Q·Δp. The shaft must deliver more because the pump loses some: Pshaft = Ph/ηpump, and the motor draws Pel = Pshaft/ηmotor. The pump head H follows from the energy equation: static lift + pressure head + all friction and minor losses.

Velocity

V = Q/A = 0.08/0.03142 = 2.546 m/s
V²/(2g) = 0.3305 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (36 + 6)·0.3305 = 13.88 m

Pump head

Both surfaces are open and practically at rest, so pressure and velocity terms drop out.

H = Δz + hL = 17 + 13.88 = 30.88 m

Answer

H = 30.88 m
9.Open-channel flow (Manning)

Answer: Q = 0.9443 m³/s

Manning’s equation (SI): for uniform flow in an open channel V = (1/n)·R2/3·S1/2 and Q = A·V, with n the roughness coefficient, S the bed slope (m/m) and R = A/P the hydraulic radius: flow area divided by wetted perimeter. Only the boundary in contact with the water counts in P, not the free surface. Rectangle: A = b·y, P = b + 2y. Trapezoid with side slopes z:1 (horizontal:vertical): A = (b + z·y)·y, P = b + 2y·√(1 + z²). A circular pipe flowing full or half full has R = D/4.

Geometry

A = (b + z·y)·y = (3 + 1.5·0.5)·0.5 = 1.875 m²
P = b + 2y·√(1 + z²) = 3 + 2·0.5·√(1 + 1.5²) = 4.803 m
R = A/P = 0.3904 m

Velocity

V = (1/0.03)·0.39042/3·0.00081/2 = 0.5036 m/s

Flow rate

Q = A·V = 1.875·0.5036 = 0.9443 m³/s

Answer

Q = 0.9443 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.005038 m/m

Manning’s equation (SI): for uniform flow in an open channel V = (1/n)·R2/3·S1/2 and Q = A·V, with n the roughness coefficient, S the bed slope (m/m) and R = A/P the hydraulic radius: flow area divided by wetted perimeter. Only the boundary in contact with the water counts in P, not the free surface. Rectangle: A = b·y, P = b + 2y. Trapezoid with side slopes z:1 (horizontal:vertical): A = (b + z·y)·y, P = b + 2y·√(1 + z²). A circular pipe flowing full or half full has R = D/4.

Geometry

A = (b + z·y)·y = (6 + 3·1.7)·1.7 = 18.87 m²
P = b + 2y·√(1 + z²) = 6 + 2·1.7·√(1 + 3²) = 16.75 m
R = A/P = 1.126 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.025·58/(18.87·1.083) = 0.07098
S = 0.07098² = 0.005038

Answer

S = 0.005038

That is a fall of 5.038 m per kilometre.

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