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 = 2 mH = 2.5 m

A vertical rectangular gate 2 m wide sits in the wall of a tank of water, with its top edge 2 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 2 mH = 2.5 mb = 2 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 2.5 mH = 1 m

A vertical rectangular gate 2 m wide sits in the wall of a tank of water, with its top edge 2.5 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 2.5 mH = 1 mb = 2 mρ = 1000 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
d1​ = 150 mmd2​ = 100 mm12p1​ − p2​ = 50 kPaQ = ?

Water flows through a horizontal venturi meter with an inlet diameter of 150 mm and a throat diameter of 100 mm. The pressure at the inlet is 50 kPa higher than at the throat. Ignoring losses, find the flow rate Q.

d1 = 150 mmd2 = 100 mmp1 − p2 = 50 kPaρ = 1000 kg/m³
Q = L/s
4.Continuity & BernoulliHard
C212 m1 md = 32 mmQ = ?

A hose with an inner diameter of 32 mm siphons water from an open tank. The highest point C of the hose is 2 m above the water surface, and the outlet (open to the air) is 1 m below the water surface. Ignore losses and take g = 9.81 m/s². Find the flow rate Q.

d = 32 mmzC = +2 mz2 = −1 mg = 9.81 m/s²
Q = L/s
5.Pipe friction & head lossMedium
V = 1.5 m/sD = 200 mmL = 200 mf = 0.022

Water flows at a mean velocity of 1.5 m/s through a pipe 200 m long with an inside diameter of 200 mm. Use the Darcy friction factor f = 0.022 and g = 9.81 m/s². Find the friction head loss hf.

V = 1.5 m/sL = 200 mD = 200 mmf = 0.022g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 5free outletH = ?L = 400 m, D = 300 mm, f = 0.0184× bend (K = 0.3)

A pipe 400 m long with an inside diameter of 300 mm (Darcy friction factor f = 0.018) 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), 4 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 120 L/s?

Q = 120 L/sL = 400 mD = 300 mmf = 0.018Kentrance = 0.5Kbend = 0.3 (×4)Kvalve = 5
H = m
7.Pumps & pump powerMedium
PQ = 10 L/sH = 50 m

A pump delivers 10 L/s of water (ρ = 1000 kg/m³) against a head of 50 m. The pump efficiency is 85% 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 = 10 L/sH = 50 mηpump = 85%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 80 L/sΔz = 6 mL = 100 m, D = 200 mm, f = 0.015, 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 6 m higher. The pipe is 100 m long with an inside diameter of 200 mm and a Darcy friction factor f = 0.015; 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 = 6 mL = 100 mD = 200 mmf = 0.015ΣK = 6
H = m
9.Open-channel flow (Manning)Medium
D = 900 mmn = 0.013, S = 0.001

A concrete storm sewer with an inside diameter of 900 mm flows half full. Manning n = 0.013 and the slope is S = 0.001. Find the flow rate Q in m³/s.

D = 900 mmn = 0.013S = 0.001
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 6 my = 2.3 m2 : 1n = 0.014, Q = 64 m³/s

A trapezoidal unfinished concrete channel with a bottom width of 6 m and side slopes of 2:1 (horizontal:vertical) must carry 64 m³/s in uniform flow at a depth of 2.3 m. Manning n = 0.014. Find the required bed slope S (in m/m).

Q = 64 m³/sb = 6 my = 2.3 mz = 2n = 0.014
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 159.4 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 + 2.5/2 = 3.25 m
A = H·b = 2.5·2 = 5 m²
gated = 2 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·3.25·5 = 159.4 kN

Answer

F = 159.4 kN
2.Hydrostatic force

Answer: ycp = 3.028 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 = 2.5 + 1/2 = 3 m
A = H·b = 1·2 = 2 m²
gated = 2.5 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·3·2 = 58.86 kN

Centre of pressure

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

Ic = b·H³/12 = 2·1³/12 = 0.1667 m⁴
ycp = yc + Ic/(yc·A) = 3 + 0.1667/(3·2) = 3.028 m

Answer

ycp = 3.028 m
3.Continuity & Bernoulli

Answer: Q = 87.67 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·(100/150)² = 0.4444·v2

Bernoulli between inlet and throat

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

p1 − p2 = ½ρv2²(1 − β⁴)
v2 = √(2·50000/(1000·(1 − 0.1975))) = 11.16 m/s
v1 = 4.961 m/s

Flow rate

Q = A2·v2 = 0.007854·11.16 = 0.08767 m³/s = 87.67 L/s

Answer

Q = 87.67 L/s
4.Continuity & Bernoulli

Answer: Q = 3.562 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·1) = √(2·9.81·1) = 4.429 m/s

Flow rate

Q = A·v = 0.0008042·4.429 = 0.003562 m³/s = 3.562 L/s

Answer

Q = 3.562 L/s
5.Pipe friction & head loss

Answer: hf = 2.523 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 head

V²/(2g) = 1.5²/(2·9.81) = 0.1147 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.022·(200/0.2)·1.5²/(2·9.81) = 2.523 m

Answer

hf = 2.523 m
6.Pipe friction & head loss

Answer: H = 4.656 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 = 0.12/0.07069 = 1.698 m/s
V²/(2g) = 0.1469 m

Loss coefficients

f·L/D = 0.018·400/0.3 = 24
ΣK = 0.5 + 4·0.3 + 5 = 6.7

Energy equation

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

H = (1 + 24 + 6.7)·0.1469 = 4.656 m

Answer

H = 4.656 m
7.Pumps & pump power

Answer: Pel = 6.074 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 = 1000·9.81·0.01·50 = 4.905 kW

Shaft power

Pshaft = 4.905/0.85 = 5.771 kW

Electrical power

Pel = 5.771/0.95 = 6.074 kW

Answer

Pel = 6.074 kW
8.Pumps & pump power

Answer: H = 10.46 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) = (7.5 + 6)·0.3305 = 4.462 m

Pump head

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

H = Δz + hL = 6 + 4.462 = 10.46 m

Answer

H = 10.46 m
9.Open-channel flow (Manning)

Answer: Q = 0.2862 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 = 0.3181 m², R = D/4 = 0.225 m

Velocity

V = (1/0.013)·0.2252/3·0.0011/2 = 0.8999 m/s

Flow rate

Q = A·V = 0.3181·0.8999 = 0.2862 m³/s

Answer

Q = 0.2862 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.0007887 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 + 2·2.3)·2.3 = 24.38 m²
P = b + 2y·√(1 + z²) = 6 + 2·2.3·√(1 + 2²) = 16.29 m
R = A/P = 1.497 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.014·64/(24.38·1.309) = 0.02808
S = 0.02808² = 0.0007887

Answer

S = 0.0007887

That is a fall of 0.7887 m per kilometre.

ExamProblems · examproblems.com/courses/hydraulic-engineering