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 2 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 = 2 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 0.5 mH = 2.5 m

A vertical rectangular gate 1.5 m wide sits in the wall of a tank of oil, with its top edge 0.5 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 0.5 mH = 2.5 mb = 1.5 mρ = 880 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
12d1​ = 100 mm, p1​ = 370 kPad2​ = 75 mm, p2​ = ?

Water flows through a horizontal pipe that narrows from 100 mm to 75 mm. In the wide section the pressure is 370 kPa and the velocity is 1.25 m/s. Ignoring losses, find the pressure p2 in the narrow section.

d1 = 100 mmd2 = 75 mmp1 = 370 kPav1 = 1.25 m/sρ = 1000 kg/m³
p2 = kPa
4.Continuity & BernoulliHard
C211.5 m1 md = 25 mmpC​ = ?

A hose with an inner diameter of 25 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 1 m below the water surface. Ignore losses and take g = 9.81 m/s². Find the absolute pressure pC at point C. The atmospheric pressure is 101.3 kPa.

d = 25 mmzC = +1.5 mz2 = −1 mg = 9.81 m/s²patm = 101.3 kPa
pC = kPa
5.Pipe friction & head lossMedium
V = 2.5 m/sD = 200 mmL = 800 mf = 0.02

Water flows at a mean velocity of 2.5 m/s through a pipe 800 m long with an inside diameter of 200 mm. Use the Darcy friction factor f = 0.02 and g = 9.81 m/s². Find the friction head loss hf.

V = 2.5 m/sL = 800 mD = 200 mmf = 0.02g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 5Δz = ?L = 200 m, D = 150 mm, f = 0.0224× 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 = 0.022. The minor losses are a square-edged entrance (K = 0.5), 4 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 60 L/s?

Q = 60 L/sL = 200 mD = 150 mmf = 0.022Kentrance = 0.5Kbend = 0.3 (×4)Kvalve = 5Kexit = 1.0
Δz = m
7.Pumps & pump powerMedium
PQ = 25 L/sH = 56 m

In a test, a pump delivers 25 L/s of water (ρ = 1000 kg/m³) against a head of 56 m while its shaft takes 17.2 kW. Use g = 9.81 m/s². Find the pump efficiency η in percent.

Q = 25 L/sH = 56 mPshaft = 17.2 kWg = 9.81 m/s²
η = %
8.Pumps & pump powerHard
PQ = 40 L/sΔz = 5 mL = 500 m, D = 150 mm, f = 0.022, ΣK = 6

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 5 m higher. The pipe is 500 m long with an inside diameter of 150 mm and a Darcy friction factor f = 0.022; the minor-loss coefficients add up to ΣK = 6 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 85%. Find the shaft power Pshaft in kW.

Q = 40 L/sΔz = 5 mL = 500 mD = 150 mmf = 0.022ΣK = 6η = 85%
Pshaft = kW
9.Open-channel flow (Manning)Medium
b = 4.5 my = 2.3 m3 : 1n = 0.03, S = 0.0005

A trapezoidal grass-lined earth channel has a bottom width of 4.5 m and side slopes of 3:1 (horizontal:vertical). Water flows uniformly 2.3 m deep. Manning n = 0.03 and the bed slope is S = 0.0005. Find the flow rate Q in m³/s.

b = 4.5 my = 2.3 mz = 3n = 0.03S = 0.0005
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 5 my = 1.2 m3 : 1n = 0.022, Q = 12 m³/s

A trapezoidal clean earth channel with a bottom width of 5 m and side slopes of 3:1 (horizontal:vertical) must carry 12 m³/s in uniform flow at a depth of 1.2 m. Manning n = 0.022. Find the required bed slope S (in m/m).

Q = 12 m³/sb = 5 my = 1.2 mz = 3n = 0.022
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 29.43 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 = 1·2 = 2 m²
gated = 1 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·1.5·2 = 29.43 kN

Answer

F = 29.43 kN
2.Hydrostatic force

Answer: ycp = 2.048 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 = 0.5 + 2.5/2 = 1.75 m
A = H·b = 2.5·1.5 = 3.75 m²
gated = 0.5 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·1.75·3.75 = 56.65 kN

Centre of pressure

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

Ic = b·H³/12 = 1.5·2.5³/12 = 1.953 m⁴
ycp = yc + Ic/(yc·A) = 1.75 + 1.953/(1.75·3.75) = 2.048 m

Answer

ycp = 2.048 m
3.Continuity & Bernoulli

Answer: p2 = 368.3 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 = 1.25·(100/75)² = 2.222 m/s
½ρ(v1² − v2²) = ½·1000·(1.25² − 2.222²)/1000 = −1.688 kPa
p2 = p1 + ½ρ(v1² − v2²) = 370 + (−1.688) = 368.3 kPa

Answer

p2 = 368.3 kPa
4.Continuity & Bernoulli

Answer: pC = 76.78 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.

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

Bernoulli from the surface to C

patm = pC + ½ρv² + ρgzC
pC = 101.3 − 1000·(4.429²/2 + 9.81·1.5)/1000 = 101.3 − 24.53 = 76.78 kPa

Answer

pC = 76.78 kPa

If this pressure falls to the vapour pressure of the water, the siphon stops working.

5.Pipe friction & head loss

Answer: hf = 25.48 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) = 2.5²/(2·9.81) = 0.3186 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.02·(800/0.2)·2.5²/(2·9.81) = 25.48 m

Answer

hf = 25.48 m
6.Pipe friction & head loss

Answer: Δz = 21.76 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 = 0.06/0.01767 = 3.395 m/s
V²/(2g) = 0.5876 m

Loss coefficients

f·L/D = 0.022·200/0.15 = 29.33
ΣK = 0.5 + 4·0.3 + 5 + 1.0 = 7.7

Total head loss

hf = 29.33·0.5876 = 17.24 m
hm = 7.7·0.5876 = 4.524 m
Δz = hf + hm = 21.76 m

Answer

Δz = 21.76 m
7.Pumps & pump power

Answer: η = 79.85 %

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 = 1000·9.81·0.025·56 = 13.73 kW

Efficiency

η = Ph/Pshaft = 13.73/17.2 = 79.85%

Answer

η = 79.85%
8.Pumps & pump power

Answer: Pshaft = 11.87 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) = (73.33 + 6)·0.2611 = 20.72 m

Pump head

H = Δz + hL = 5 + 20.72 = 25.72 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.04·25.72/0.85 = 11.87 kW

Answer

Pshaft = 11.87 kW
9.Open-channel flow (Manning)

Answer: Q = 24.18 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 = (4.5 + 3·2.3)·2.3 = 26.22 m²
P = b + 2y·√(1 + z²) = 4.5 + 2·2.3·√(1 + 3²) = 19.05 m
R = A/P = 1.377 m

Velocity

V = (1/0.03)·1.3772/3·0.00051/2 = 0.9224 m/s

Flow rate

Q = A·V = 26.22·0.9224 = 24.18 m³/s

Answer

Q = 24.18 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.000853 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 = (5 + 3·1.2)·1.2 = 10.32 m²
P = b + 2y·√(1 + z²) = 5 + 2·1.2·√(1 + 3²) = 12.59 m
R = A/P = 0.8197 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.022·12/(10.32·0.8759) = 0.02921
S = 0.02921² = 0.000853

Answer

S = 0.000853

That is a fall of 0.853 m per kilometre.

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