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 mH = 1 m

A vertical rectangular gate 1 m wide sits in the wall of a tank of water, with its top edge 1 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 1 mH = 1 mb = 1 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 4 mH = 1 m

A vertical rectangular gate 1 m wide sits in the wall of a tank of water, with its top edge 4 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 4 mH = 1 mb = 1 mρ = 1000 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
Q = ?d = 40 mm, Cd​ = 0.6h = 6 m

Water drains from a large open tank through a sharp-edged orifice with a diameter of 40 mm. The water level is kept 6 m above the orifice and the discharge coefficient is 0.6. Find the flow rate Q. Use g = 9.81 m/s².

d = 40 mmh = 6 mCd = 0.6g = 9.81 m/s²
Q = L/s
4.Continuity & BernoulliHard
12d1​ = 200 mm, p1​ = 310 kPad2​ = 100 mm, p2​ = ?Δz = 10 m

Water flows up through a pipe that narrows from 200 mm to 100 mm while rising 10 m. At section 1 the pressure is 310 kPa and the velocity is 2.25 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 200 mmd2 = 100 mmp1 = 310 kPav1 = 2.25 m/sΔz = 10 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
Q = 120 L/sD = 300 mmL = 800 mf = 0.03

Water flows at 120 L/s through a pipe 800 m long with an inside diameter of 300 mm. Use the Darcy friction factor f = 0.03 and g = 9.81 m/s². Find the friction head loss hf.

Q = 120 L/sL = 800 mD = 300 mmf = 0.03g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 5free outletH = ?L = 150 m, D = 100 mm, f = 0.0183× bend (K = 0.3)

A pipe 150 m long with an inside diameter of 100 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), 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 12 L/s?

Q = 12 L/sL = 150 mD = 100 mmf = 0.018Kentrance = 0.5Kbend = 0.3 (×3)Kvalve = 5
H = m
7.Pumps & pump powerMedium
PQ = 20 L/sH = 28 m

A pump delivers 20 L/s of water (ρ = 1000 kg/m³) against a head of 28 m. The pump efficiency is 78% 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 = 20 L/sH = 28 mηpump = 78%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 40 L/sΔz = 8 mL = 200 m, D = 150 mm, f = 0.02, ΣK = 4

A pump moves 40 L/s of water (ρ = 1000 kg/m³) from an open lower reservoir to an upper tank whose water surface is 8 m higher. The pipe is 200 m long with an inside diameter of 150 mm and a Darcy friction factor f = 0.02; the minor-loss coefficients add up to ΣK = 4 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 78%. Find the shaft power Pshaft in kW.

Q = 40 L/sΔz = 8 mL = 200 mD = 150 mmf = 0.02ΣK = 4η = 78%
Pshaft = kW
9.Open-channel flow (Manning)Medium
D = 1200 mmn = 0.013, S = 0.0008

A concrete storm sewer with an inside diameter of 1200 mm flows half full. Manning n = 0.013 and the slope is S = 0.0008. Find the flow rate Q in m³/s.

D = 1200 mmn = 0.013S = 0.0008
Q = m³/s
10.Open-channel flow (Manning)Hard
D = 450 mmn = 0.013, V = 0.75 m/s

A concrete sewer with an inside diameter of 450 mm (Manning n = 0.013) must reach a self-cleansing velocity of 0.75 m/s when flowing just full. Find the minimum slope S (in m/m).

D = 450 mmn = 0.013V = 0.75 m/s
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 14.71 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 + 1/2 = 1.5 m
A = H·b = 1·1 = 1 m²
gated = 1 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·1.5·1 = 14.71 kN

Answer

F = 14.71 kN
2.Hydrostatic force

Answer: ycp = 4.519 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 = 4 + 1/2 = 4.5 m
A = H·b = 1·1 = 1 m²
gated = 4 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·4.5·1 = 44.15 kN

Centre of pressure

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

Ic = b·H³/12 = 1·1³/12 = 0.08333 m⁴
ycp = yc + Ic/(yc·A) = 4.5 + 0.08333/(4.5·1) = 4.519 m

Answer

ycp = 4.519 m
3.Continuity & Bernoulli

Answer: Q = 8.181 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.

Ideal jet velocity

√(2gh) = √(2·9.81·6) = 10.85 m/s

Actual flow rate

The discharge coefficient accounts for the contraction of the jet and friction at the edge.

Q = Cd·A·√(2gh) = 0.6·0.001257·10.85 = 0.008181 m³/s = 8.181 L/s

Answer

Q = 8.181 L/s
4.Continuity & Bernoulli

Answer: p2 = 173.9 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 = 2.25·(200/100)² = 9 m/s
½ρ(v1² − v2²) = ½·1000·(2.25² − 9²)/1000 = −37.97 kPa
ρgΔz = 1000·9.81·10/1000 = 98.1 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 310 + (−37.97) − 98.1 = 173.9 kPa

Answer

p2 = 173.9 kPa
5.Pipe friction & head loss

Answer: hf = 11.75 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·0.3²/4 = 0.07069 m²
V = Q/A = 0.12/0.07069 = 1.698 m/s

Velocity head

V²/(2g) = 1.698²/(2·9.81) = 0.1469 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.03·(800/0.3)·1.698²/(2·9.81) = 11.75 m

Answer

hf = 11.75 m
6.Pipe friction & head loss

Answer: H = 4.093 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 = 0.012/0.007854 = 1.528 m/s
V²/(2g) = 0.119 m

Loss coefficients

f·L/D = 0.018·150/0.1 = 27
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 + 27 + 6.4)·0.119 = 4.093 m

Answer

H = 4.093 m
7.Pumps & pump power

Answer: Pel = 7.414 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 = 1000·9.81·0.02·28 = 5.494 kW

Shaft power

Pshaft = 5.494/0.78 = 7.043 kW

Electrical power

Pel = 7.043/0.95 = 7.414 kW

Answer

Pel = 7.414 kW
8.Pumps & pump power

Answer: Pshaft = 8.053 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 = 0.04/0.01767 = 2.264 m/s
V²/(2g) = 0.2611 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (26.67 + 4)·0.2611 = 8.008 m

Pump head

H = Δz + hL = 8 + 8.008 = 16.01 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.04·16.01/0.78 = 8.053 kW

Answer

Pshaft = 8.053 kW
9.Open-channel flow (Manning)

Answer: Q = 0.5514 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 = 0.5655 m², R = D/4 = 0.3 m

Velocity

V = (1/0.013)·0.32/3·0.00081/2 = 0.975 m/s

Flow rate

Q = A·V = 0.5655·0.975 = 0.5514 m³/s

Answer

Q = 0.5514 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.00175 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 = 0.45/4 = 0.1125 m

Solve Manning for S

S = (n·V/R2/3)² = (0.013·0.75/0.233)² = 0.00175

Answer

S = 0.00175

That is a fall of 1.75 m per kilometre.

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