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 = 4 mH = 2.5 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 resultant hydrostatic force F on the gate.

d = 4 mH = 2.5 mb = 1 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 2 mH = 1 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 resultant hydrostatic force F on the gate.

d = 2 mH = 1 mb = 1 mρ = 880 kg/m³g = 9.81 m/s²
F = kN
3.Continuity & BernoulliMedium
12d1​ = 200 mm, p1​ = ?d2​ = 150 mm, p2​ = 200 kPa

Water flows at 19 L/s through a horizontal pipe that narrows from 200 mm to 150 mm. The pressure in the narrow section is 200 kPa. Ignoring losses, find the pressure p1 in the wide section.

Q = 19 L/sd1 = 200 mmd2 = 150 mmp2 = 200 kPaρ = 1000 kg/m³
p1 = kPa
4.Continuity & BernoulliHard
12d1​ = 200 mm, p1​ = 260 kPad2​ = 75 mm, p2​ = ?Δz = 9 m

Water flows up through a pipe that narrows from 200 mm to 75 mm while rising 9 m. At section 1 the pressure is 260 kPa and the velocity is 0.75 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 200 mmd2 = 75 mmp1 = 260 kPav1 = 0.75 m/sΔz = 9 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
V = 2.3 m/sD = 100 mmL = 50 mf = 0.03

Water (ρ = 1000 kg/m³) flows at 2.3 m/s through a horizontal pipe, 50 m long, with an inside diameter of 100 mm. Use the Darcy friction factor f = 0.03 and g = 9.81 m/s². Find the pressure drop Δp over the pipe in kPa.

V = 2.3 m/sL = 50 mD = 100 mmf = 0.03ρ = 1000 kg/m³
Δp = kPa
6.Pipe friction & head lossHard
K = 5Δz = ?L = 500 m, D = 300 mm, f = 0.0152× bend (K = 0.3)

Two open reservoirs are joined by a pipe 500 m long with an inside diameter of 300 mm and a Darcy friction factor f = 0.015. The minor losses are a square-edged entrance (K = 0.5), 2 bends (K = 0.3 each), a valve (K = 5) 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 100 L/s?

Q = 100 L/sL = 500 mD = 300 mmf = 0.015Kentrance = 0.5Kbend = 0.3 (×2)Kvalve = 5Kexit = 1.0
Δz = m
7.Pumps & pump powerMedium
PQ = 10 L/sH = 76 m

A pump delivers 10 L/s of water (ρ = 1000 kg/m³) against a head of 76 m. The pump efficiency is 82% 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 = 76 mηpump = 82%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 60 L/sΔz = 7 mL = 150 m, D = 250 mm, f = 0.025, ΣK = 6

A pump moves 60 L/s of water (ρ = 1000 kg/m³) from an open lower reservoir to an upper tank whose water surface is 7 m higher. The pipe is 150 m long with an inside diameter of 250 mm and a Darcy friction factor f = 0.025; 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 = 60 L/sΔz = 7 mL = 150 mD = 250 mmf = 0.025ΣK = 6
H = m
9.Open-channel flow (Manning)Medium
b = 3.5 my = 2.2 mn = 0.012, S = 0.001

A rectangular finished concrete channel is 3.5 m wide. Water flows uniformly 2.2 m deep. Manning n = 0.012 and the bed slope is S = 0.001. Find the flow rate Q in m³/s.

b = 3.5 my = 2.2 mn = 0.012S = 0.001
Q = m³/s
10.Open-channel flow (Manning)Hard
D = 300 mmn = 0.013, V = 0.6 m/s

A concrete sewer with an inside diameter of 300 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 = 300 mmn = 0.013V = 0.6 m/s
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 128.8 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 = 4 + 2.5/2 = 5.25 m
A = H·b = 2.5·1 = 2.5 m²
gated = 4 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·5.25·2.5 = 128.8 kN

Answer

F = 128.8 kN
2.Hydrostatic force

Answer: F = 21.58 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 + 1/2 = 2.5 m
A = H·b = 1·1 = 1 m²
gated = 2 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·2.5·1 = 21.58 kN

Answer

F = 21.58 kN
3.Continuity & Bernoulli

Answer: p1 = 200.4 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 = 0.019/0.03142 = 0.6048 m/s
v2 = Q/A2 = 0.019/0.01767 = 1.075 m/s

Bernoulli

p1 = p2 + ½ρ(v2² − v1²) = 200 + ½·1000·(1.075² − 0.6048²)/1000 = 200 + 0.3951 = 200.4 kPa

Answer

p1 = 200.4 kPa
4.Continuity & Bernoulli

Answer: p2 = 157.8 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 = 0.75·(200/75)² = 5.333 m/s
½ρ(v1² − v2²) = ½·1000·(0.75² − 5.333²)/1000 = −13.94 kPa
ρgΔz = 1000·9.81·9/1000 = 88.29 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 260 + (−13.94) − 88.29 = 157.8 kPa

Answer

p2 = 157.8 kPa
5.Pipe friction & head loss

Answer: Δp = 39.67 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) = 0.03·(50/0.1)·2.3²/(2·9.81) = 4.044 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 = 1000·9.81·4.044 = 39675 Pa = 39.67 kPa

Answer

Δp = 39.67 kPa
6.Pipe friction & head loss

Answer: Δz = 3.274 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 = 0.1/0.07069 = 1.415 m/s
V²/(2g) = 0.102 m

Loss coefficients

f·L/D = 0.015·500/0.3 = 25
ΣK = 0.5 + 2·0.3 + 5 + 1.0 = 7.1

Total head loss

hf = 25·0.102 = 2.55 m
hm = 7.1·0.102 = 0.7243 m
Δz = hf + hm = 3.274 m

Answer

Δz = 3.274 m
7.Pumps & pump power

Answer: Pel = 9.571 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 = 1000·9.81·0.01·76 = 7.456 kW

Shaft power

Pshaft = 7.456/0.82 = 9.092 kW

Electrical power

Pel = 9.092/0.95 = 9.571 kW

Answer

Pel = 9.571 kW
8.Pumps & pump power

Answer: H = 8.599 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 = 0.06/0.04909 = 1.222 m/s
V²/(2g) = 0.07615 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (15 + 6)·0.07615 = 1.599 m

Pump head

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

H = Δz + hL = 7 + 1.599 = 8.599 m

Answer

H = 8.599 m
9.Open-channel flow (Manning)

Answer: Q = 19.95 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·y = 3.5·2.2 = 7.7 m²
P = b + 2y = 3.5 + 2·2.2 = 7.9 m
R = A/P = 0.9747 m

Velocity

V = (1/0.012)·0.97472/3·0.0011/2 = 2.591 m/s

Flow rate

Q = A·V = 7.7·2.591 = 19.95 m³/s

Answer

Q = 19.95 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.001924 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 = 0.3/4 = 0.075 m

Solve Manning for S

S = (n·V/R2/3)² = (0.013·0.6/0.1778)² = 0.001924

Answer

S = 0.001924

That is a fall of 1.924 m per kilometre.

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