Hydraulic Engineering: cram pack

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

New problemsBack to the course

In the print window, choose “Save as PDF” to keep a copy on your device.

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 = 4 mH = 2.5 m

A vertical rectangular gate 1.5 m wide sits in the wall of a tank of water, with its top edge 4 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 4 mH = 2.5 mb = 1.5 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 2.5 mH = 2.5 m

A vertical rectangular gate 3 m wide sits in the wall of a tank of oil, with its top edge 2.5 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 2.5 mH = 2.5 mb = 3 mρ = 880 kg/m³g = 9.81 m/s²
F = kN
3.Continuity & BernoulliMedium
d1​ = 100 mmd2​ = 60 mm12p1​ − p2​ = 20 kPaQ = ?

Water flows through a horizontal venturi meter with an inlet diameter of 100 mm and a throat diameter of 60 mm. The pressure at the inlet is 20 kPa higher than at the throat. Ignoring losses, find the flow rate Q.

d1 = 100 mmd2 = 60 mmp1 − p2 = 20 kPaρ = 1000 kg/m³
Q = L/s
4.Continuity & BernoulliHard
C211.5 m4 md = 40 mmQ = ?

A hose with an inner diameter of 40 mm siphons water from an open tank. The highest point C of the hose is 1.5 m above the water surface, and the outlet (open to the air) is 4 m below the water surface. Ignore losses and take g = 9.81 m/s². Find the flow rate Q.

d = 40 mmzC = +1.5 mz2 = −4 mg = 9.81 m/s²
Q = L/s
5.Pipe friction & head lossMedium
Q = 4 L/sD = 50 mmL = 50 mf = 0.022

Water flows at 4 L/s through a pipe 50 m long with an inside diameter of 50 mm. Use the Darcy friction factor f = 0.022 and g = 9.81 m/s². Find the friction head loss hf.

Q = 4 L/sL = 50 mD = 50 mmf = 0.022g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 10Δz = 27 mL = 100 m, D = 150 mm, f = 0.0222× bend (K = 0.3)

Two open reservoirs are joined by a pipe 100 m long with an inside diameter of 150 mm and a Darcy friction factor f = 0.022. The water surface of the upper reservoir is 27 m above that of the lower one. The minor losses are a square-edged entrance (K = 0.5), 2 bends (K = 0.3 each), a valve (K = 10) and the exit into the lower reservoir (K = 1.0). Use g = 9.81 m/s². Find the flow rate Q in L/s.

Δz = 27 mL = 100 mD = 150 mmf = 0.022Kentrance = 0.5Kbend = 0.3 (×2)Kvalve = 10Kexit = 1.0
Q = L/s
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 80% 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 = 80%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 100 L/sΔz = 9 mL = 200 m, D = 250 mm, f = 0.015, ΣK = 8

A pump moves 100 L/s of water (ρ = 1000 kg/m³) from an open lower reservoir to an upper tank whose water surface is 9 m higher. The pipe is 200 m long with an inside diameter of 250 mm and a Darcy friction factor f = 0.015; the minor-loss coefficients add up to ΣK = 8 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 80%. Find the shaft power Pshaft in kW.

Q = 100 L/sΔz = 9 mL = 200 mD = 250 mmf = 0.015ΣK = 8η = 80%
Pshaft = kW
9.Open-channel flow (Manning)Medium
b = 5.5 my = 1.4 m3 : 1n = 0.015, S = 0.002

A trapezoidal brickwork channel has a bottom width of 5.5 m and side slopes of 3:1 (horizontal:vertical). Water flows uniformly 1.4 m deep. Manning n = 0.015 and the bed slope is S = 0.002. Find the flow rate Q in m³/s.

b = 5.5 my = 1.4 mz = 3n = 0.015S = 0.002
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 1 my = 1 mn = 0.03, Q = 0.88 m³/s

A rectangular grass-lined earth channel 1 m wide must carry 0.88 m³/s in uniform flow at a depth of 1 m. Manning n = 0.03. Find the required bed slope S (in m/m).

Q = 0.88 m³/sb = 1 my = 1 mn = 0.03
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 193.1 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 = 4 + 2.5/2 = 5.25 m
A = H·b = 2.5·1.5 = 3.75 m²
gated = 4 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·5.25·3.75 = 193.1 kN

Answer

F = 193.1 kN
2.Hydrostatic force

Answer: F = 242.8 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 = 2.5 + 2.5/2 = 3.75 m
A = H·b = 2.5·3 = 7.5 m²
gated = 2.5 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·3.75·7.5 = 242.8 kN

Answer

F = 242.8 kN
3.Continuity & Bernoulli

Answer: Q = 19.17 L/s

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

v1 = v2·(60/100)² = 0.36·v2

Bernoulli between inlet and throat

The pipe is horizontal, so only pressure and velocity change.

p1 − p2 = ½ρv2²(1 − β⁴)
v2 = √(2·20000/(1000·(1 − 0.1296))) = 6.779 m/s
v1 = 2.44 m/s

Flow rate

Q = A2·v2 = 0.002827·6.779 = 0.01917 m³/s = 19.17 L/s

Answer

Q = 19.17 L/s
4.Continuity & Bernoulli

Answer: Q = 11.13 L/s

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.

Velocity in the hose

Surface and outlet are both open to the air, so the pressure terms cancel.

v = √(2g·4) = √(2·9.81·4) = 8.859 m/s

Flow rate

Q = A·v = 0.001257·8.859 = 0.01113 m³/s = 11.13 L/s

Answer

Q = 11.13 L/s
5.Pipe friction & head loss

Answer: hf = 4.654 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.

Mean velocity

A = π·0.05²/4 = 0.001963 m²
V = Q/A = 0.004/0.001963 = 2.037 m/s

Velocity head

V²/(2g) = 2.037²/(2·9.81) = 0.2115 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.022·(50/0.05)·2.037²/(2·9.81) = 4.654 m

Answer

hf = 4.654 m
6.Pipe friction & head loss

Answer: Q = 78.62 L/s

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.

Loss coefficients

f·L/D = 0.022·100/0.15 = 14.67
ΣK = 0.5 + 2·0.3 + 10 + 1.0 = 12.1

Energy equation

Both surfaces are open to the air and practically at rest, so all of Δz is lost in the pipe.

27 = (14.67 + 12.1)·V²/(2·9.81)
V = √(2·9.81·27/26.77) = 4.449 m/s

Flow rate

Q = V·π·D²/4 = 4.449·0.01767 = 0.07862 m³/s = 78.62 L/s

Answer

Q = 78.62 L/s
7.Pumps & pump power

Answer: Pel = 50.34 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 = 38.26/0.8 = 47.82 kW

Electrical power

Pel = 47.82/0.95 = 50.34 kW

Answer

Pel = 50.34 kW
8.Pumps & pump power

Answer: Pshaft = 16.22 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.

Velocity

V = Q/A = 0.1/0.04909 = 2.037 m/s
V²/(2g) = 0.2115 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (12 + 8)·0.2115 = 4.23 m

Pump head

H = Δz + hL = 9 + 4.23 = 13.23 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.1·13.23/0.8 = 16.22 kW

Answer

Pshaft = 16.22 kW
9.Open-channel flow (Manning)

Answer: Q = 39.02 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 = (5.5 + 3·1.4)·1.4 = 13.58 m²
P = b + 2y·√(1 + z²) = 5.5 + 2·1.4·√(1 + 3²) = 14.35 m
R = A/P = 0.9461 m

Velocity

V = (1/0.015)·0.94612/3·0.0021/2 = 2.873 m/s

Flow rate

Q = A·V = 13.58·2.873 = 39.02 m³/s

Answer

Q = 39.02 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.003016 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·y = 1·1 = 1 m²
P = b + 2y = 1 + 2·1 = 3 m
R = A/P = 0.3333 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.03·0.88/(1·0.4807) = 0.05491
S = 0.05491² = 0.003016

Answer

S = 0.003016

That is a fall of 3.016 m per kilometre.

ExamProblems · examproblems.com/courses/hydraulic-engineering