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 = 1.5 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 1.5 m below the surface. Find the resultant hydrostatic force F on the gate.

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

A vertical rectangular gate 1 m wide sits in the wall of a tank of oil, with its top edge 2 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 2 mH = 2 mb = 1 mρ = 880 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
d1​ = 80 mmd2​ = 40 mm12p1​ − p2​ = 22 kPaQ = ?

Water flows through a horizontal venturi meter with an inlet diameter of 80 mm and a throat diameter of 40 mm. The pressure at the inlet is 22 kPa higher than at the throat. Ignoring losses, find the flow rate Q.

d1 = 80 mmd2 = 40 mmp1 − p2 = 22 kPaρ = 1000 kg/m³
Q = L/s
4.Continuity & BernoulliHard
12d1​ = 75 mm, p1​ = 320 kPad2​ = 25 mm, p2​ = ?Δz = 6 m

Water flows up through a pipe that narrows from 75 mm to 25 mm while rising 6 m. At section 1 the pressure is 320 kPa and the velocity is 1.5 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 75 mmd2 = 25 mmp1 = 320 kPav1 = 1.5 m/sΔz = 6 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
V = 1.3 m/sD = 150 mmL = 1000 mf = 0.018

Water flows at a mean velocity of 1.3 m/s through a pipe 1000 m long with an inside diameter of 150 mm. Use the Darcy friction factor f = 0.018 and g = 9.81 m/s². Find the friction head loss hf.

V = 1.3 m/sL = 1000 mD = 150 mmf = 0.018g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 2Δz = ?L = 200 m, D = 150 mm, f = 0.023× bend (K = 0.3)

Two open reservoirs are joined by a pipe 200 m long with an inside diameter of 150 mm and a Darcy friction factor f = 0.02. The minor losses are a square-edged entrance (K = 0.5), 3 bends (K = 0.3 each), a valve (K = 2) and the exit into the lower reservoir (K = 1.0). Use g = 9.81 m/s². What difference in water level Δz between the reservoirs gives a flow rate of 40 L/s?

Q = 40 L/sL = 200 mD = 150 mmf = 0.02Kentrance = 0.5Kbend = 0.3 (×3)Kvalve = 2Kexit = 1.0
Δz = m
7.Pumps & pump powerMedium
PQ = 20 L/sH = 54 m

A pump delivers 20 L/s of water (ρ = 1000 kg/m³) against a head of 54 m. The pump efficiency is 78% and the electric motor driving it has an efficiency of 90%. Use g = 9.81 m/s². Find the electrical power Pel the motor draws, in kW.

Q = 20 L/sH = 54 mηpump = 78%ηmotor = 90%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 80 L/sΔz = 5 mL = 150 m, D = 250 mm, f = 0.022, ΣK = 5

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 5 m higher. The pipe is 150 m long with an inside diameter of 250 mm and a Darcy friction factor f = 0.022; the minor-loss coefficients add up to ΣK = 5 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 80%. Find the shaft power Pshaft in kW.

Q = 80 L/sΔz = 5 mL = 150 mD = 250 mmf = 0.022ΣK = 5η = 80%
Pshaft = kW
9.Open-channel flow (Manning)Medium
D = 600 mmn = 0.013, S = 0.0008

A concrete storm sewer with an inside diameter of 600 mm flows half full. Manning n = 0.013 and the slope is S = 0.0008. Find the flow rate Q in m³/s.

D = 600 mmn = 0.013S = 0.0008
Q = m³/s
10.Open-channel flow (Manning)Hard
D = 375 mmn = 0.013, V = 0.6 m/s

A concrete sewer with an inside diameter of 375 mm (Manning n = 0.013) must reach a self-cleansing velocity of 0.6 m/s when flowing just full. Find the minimum slope S (in m/m).

D = 375 mmn = 0.013V = 0.6 m/s
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 49.66 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 = 1.5 + 1.5/2 = 2.25 m
A = H·b = 1.5·1.5 = 2.25 m²
gated = 1.5 mH = 1.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·2.25·2.25 = 49.66 kN

Answer

F = 49.66 kN
2.Hydrostatic force

Answer: ycp = 3.111 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 + 2/2 = 3 m
A = H·b = 2·1 = 2 m²
gated = 2 mH = 2 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·3·2 = 51.8 kN

Centre of pressure

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

Ic = b·H³/12 = 1·2³/12 = 0.6667 m⁴
ycp = yc + Ic/(yc·A) = 3 + 0.6667/(3·2) = 3.111 m

Answer

ycp = 3.111 m
3.Continuity & Bernoulli

Answer: Q = 8.609 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·(40/80)² = 0.25·v2

Bernoulli between inlet and throat

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

p1 − p2 = ½ρv2²(1 − β⁴)
v2 = √(2·22000/(1000·(1 − 0.0625))) = 6.851 m/s
v1 = 1.713 m/s

Flow rate

Q = A2·v2 = 0.001257·6.851 = 0.008609 m³/s = 8.609 L/s

Answer

Q = 8.609 L/s
4.Continuity & Bernoulli

Answer: p2 = 171.1 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 = 1.5·(75/25)² = 13.5 m/s
½ρ(v1² − v2²) = ½·1000·(1.5² − 13.5²)/1000 = −90 kPa
ρgΔz = 1000·9.81·6/1000 = 58.86 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 320 + (−90) − 58.86 = 171.1 kPa

Answer

p2 = 171.1 kPa
5.Pipe friction & head loss

Answer: hf = 10.34 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) = 1.3²/(2·9.81) = 0.08614 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.018·(1000/0.15)·1.3²/(2·9.81) = 10.34 m

Answer

hf = 10.34 m
6.Pipe friction & head loss

Answer: Δz = 8.113 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 = 0.04/0.01767 = 2.264 m/s
V²/(2g) = 0.2611 m

Loss coefficients

f·L/D = 0.02·200/0.15 = 26.67
ΣK = 0.5 + 3·0.3 + 2 + 1.0 = 4.4

Total head loss

hf = 26.67·0.2611 = 6.964 m
hm = 4.4·0.2611 = 1.149 m
Δz = hf + hm = 8.113 m

Answer

Δz = 8.113 m
7.Pumps & pump power

Answer: Pel = 15.09 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 = 1000·9.81·0.02·54 = 10.59 kW

Shaft power

Pshaft = 10.59/0.78 = 13.58 kW

Electrical power

Pel = 13.58/0.9 = 15.09 kW

Answer

Pel = 15.09 kW
8.Pumps & pump power

Answer: Pshaft = 7.322 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 = 0.08/0.04909 = 1.63 m/s
V²/(2g) = 0.1354 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (13.2 + 5)·0.1354 = 2.464 m

Pump head

H = Δz + hL = 5 + 2.464 = 7.464 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.08·7.464/0.8 = 7.322 kW

Answer

Pshaft = 7.322 kW
9.Open-channel flow (Manning)

Answer: Q = 0.08683 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 = 0.1414 m², R = D/4 = 0.15 m

Velocity

V = (1/0.013)·0.152/3·0.00081/2 = 0.6142 m/s

Flow rate

Q = A·V = 0.1414·0.6142 = 0.08683 m³/s

Answer

Q = 0.08683 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.001429 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.

Hydraulic radius

R = D/4 = 0.375/4 = 0.09375 m

Solve Manning for S

S = (n·V/R2/3)² = (0.013·0.6/0.2064)² = 0.001429

Answer

S = 0.001429

That is a fall of 1.429 m per kilometre.

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