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 = 2.5 mH = 1.5 m

A vertical rectangular gate 1 m wide sits in the wall of a tank of water, with its top edge 2.5 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 2.5 mH = 1.5 mb = 1 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 1.5 mH = 1 m

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

d = 1.5 mH = 1 mb = 1.5 mρ = 880 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
12d1​ = 150 mm, p1​ = 300 kPad2​ = 100 mm, p2​ = ?

Water flows through a horizontal pipe that narrows from 150 mm to 100 mm. In the wide section the pressure is 300 kPa and the velocity is 1.75 m/s. Ignoring losses, find the pressure p2 in the narrow section.

d1 = 150 mmd2 = 100 mmp1 = 300 kPav1 = 1.75 m/sρ = 1000 kg/m³
p2 = kPa
4.Continuity & BernoulliHard
12d1​ = 150 mm, p1​ = 120 kPad2​ = 100 mm, p2​ = ?Δz = 2 m

Water flows up through a pipe that narrows from 150 mm to 100 mm while rising 2 m. At section 1 the pressure is 120 kPa and the velocity is 1.25 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 150 mmd2 = 100 mmp1 = 120 kPav1 = 1.25 m/sΔz = 2 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
V = 2 m/sD = 300 mmL = 800 mf = 0.028

Water (ρ = 1000 kg/m³) flows at 2 m/s through a horizontal pipe, 800 m long, with an inside diameter of 300 mm. Use the Darcy friction factor f = 0.028 and g = 9.81 m/s². Find the pressure drop Δp over the pipe in kPa.

V = 2 m/sL = 800 mD = 300 mmf = 0.028ρ = 1000 kg/m³
Δp = kPa
6.Pipe friction & head lossHard
K = 10Δz = 36 mL = 200 m, D = 250 mm, f = 0.0184× bend (K = 0.3)

Two open reservoirs are joined by a pipe 200 m long with an inside diameter of 250 mm and a Darcy friction factor f = 0.018. The water surface of the upper reservoir is 36 m above that of the lower one. The minor losses are a square-edged entrance (K = 0.5), 4 bends (K = 0.3 each), a valve (K = 10) and the exit into the lower reservoir (K = 1.0). Use g = 9.81 m/s². Find the flow rate Q in L/s.

Δz = 36 mL = 200 mD = 250 mmf = 0.018Kentrance = 0.5Kbend = 0.3 (×4)Kvalve = 10Kexit = 1.0
Q = L/s
7.Pumps & pump powerMedium
PQ = 40 L/sH = 58 m

In a test, a pump delivers 40 L/s of water (ρ = 1000 kg/m³) against a head of 58 m while its shaft takes 26.8 kW. Use g = 9.81 m/s². Find the pump efficiency η in percent.

Q = 40 L/sH = 58 mPshaft = 26.8 kWg = 9.81 m/s²
η = %
8.Pumps & pump powerHard
PQ = 60 L/sΔz = 13 mL = 200 m, D = 200 mm, f = 0.015, 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 13 m higher. The pipe is 200 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. The pump efficiency is 70%. Find the shaft power Pshaft in kW.

Q = 60 L/sΔz = 13 mL = 200 mD = 200 mmf = 0.015ΣK = 6η = 70%
Pshaft = kW
9.Open-channel flow (Manning)Medium
b = 2 my = 1.8 m3 : 1n = 0.022, S = 0.002

A trapezoidal clean earth channel has a bottom width of 2 m and side slopes of 3:1 (horizontal:vertical). Water flows uniformly 1.8 m deep. Manning n = 0.022 and the bed slope is S = 0.002. Find the flow rate Q in m³/s.

b = 2 my = 1.8 mz = 3n = 0.022S = 0.002
Q = m³/s
10.Open-channel flow (Manning)Hard
D = 300 mmn = 0.013, V = 1.2 m/s

A concrete sewer with an inside diameter of 300 mm (Manning n = 0.013) must reach a self-cleansing velocity of 1.2 m/s when flowing just full. Find the minimum slope S (in m/m).

D = 300 mmn = 0.013V = 1.2 m/s
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 47.82 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 = 2.5 + 1.5/2 = 3.25 m
A = H·b = 1.5·1 = 1.5 m²
gated = 2.5 mH = 1.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·3.25·1.5 = 47.82 kN

Answer

F = 47.82 kN
2.Hydrostatic force

Answer: ycp = 2.042 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 = 1.5 + 1/2 = 2 m
A = H·b = 1·1.5 = 1.5 m²
gated = 1.5 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·2·1.5 = 25.9 kN

Centre of pressure

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

Ic = b·H³/12 = 1.5·1³/12 = 0.125 m⁴
ycp = yc + Ic/(yc·A) = 2 + 0.125/(2·1.5) = 2.042 m

Answer

ycp = 2.042 m
3.Continuity & Bernoulli

Answer: p2 = 293.8 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 = 1.75·(150/100)² = 3.938 m/s
½ρ(v1² − v2²) = ½·1000·(1.75² − 3.938²)/1000 = −6.221 kPa
p2 = p1 + ½ρ(v1² − v2²) = 300 + (−6.221) = 293.8 kPa

Answer

p2 = 293.8 kPa
4.Continuity & Bernoulli

Answer: p2 = 97.21 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·(150/100)² = 2.813 m/s
½ρ(v1² − v2²) = ½·1000·(1.25² − 2.813²)/1000 = −3.174 kPa
ρgΔz = 1000·9.81·2/1000 = 19.62 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 120 + (−3.174) − 19.62 = 97.21 kPa

Answer

p2 = 97.21 kPa
5.Pipe friction & head loss

Answer: Δp = 149.3 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) = 0.028·(800/0.3)·2²/(2·9.81) = 15.22 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 = 1000·9.81·15.22 = 149333 Pa = 149.3 kPa

Answer

Δp = 149.3 kPa
6.Pipe friction & head loss

Answer: Q = 250.6 L/s

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.

Loss coefficients

f·L/D = 0.018·200/0.25 = 14.4
ΣK = 0.5 + 4·0.3 + 10 + 1.0 = 12.7

Energy equation

Both surfaces are open to the air and practically at rest, so all of Δz is lost in the pipe.

36 = (14.4 + 12.7)·V²/(2·9.81)
V = √(2·9.81·36/27.1) = 5.105 m/s

Flow rate

Q = V·π·D²/4 = 5.105·0.04909 = 0.2506 m³/s = 250.6 L/s

Answer

Q = 250.6 L/s
7.Pumps & pump power

Answer: η = 84.92 %

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 = 1000·9.81·0.04·58 = 22.76 kW

Efficiency

η = Ph/Pshaft = 22.76/26.8 = 84.92%

Answer

η = 84.92%
8.Pumps & pump power

Answer: Pshaft = 14.21 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 = 0.06/0.03142 = 1.91 m/s
V²/(2g) = 0.1859 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (15 + 6)·0.1859 = 3.904 m

Pump head

H = Δz + hL = 13 + 3.904 = 16.9 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.06·16.9/0.7 = 14.21 kW

Answer

Pshaft = 14.21 kW
9.Open-channel flow (Manning)

Answer: Q = 26.99 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 = (2 + 3·1.8)·1.8 = 13.32 m²
P = b + 2y·√(1 + z²) = 2 + 2·1.8·√(1 + 3²) = 13.38 m
R = A/P = 0.9952 m

Velocity

V = (1/0.022)·0.99522/3·0.0021/2 = 2.026 m/s

Flow rate

Q = A·V = 13.32·2.026 = 26.99 m³/s

Answer

Q = 26.99 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.007694 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 = (0.013·1.2/0.1778)² = 0.007694

Answer

S = 0.007694

That is a fall of 7.694 m per kilometre.

ExamProblems · examproblems.com/courses/hydraulic-engineering