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 = 3 mH = 1.5 m

A vertical rectangular gate 1 m wide sits in the wall of a tank of water, with its top edge 3 m below the surface. Find the resultant hydrostatic force F on the gate.

d = 3 mH = 1.5 mb = 1 mρ = 1000 kg/m³g = 9.81 m/s²
F = kN
2.Hydrostatic forceHard
gated = 3 mH = 3 m

A vertical rectangular gate 2 m wide sits in the wall of a tank of oil, with its top edge 3 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 3 mH = 3 mb = 2 mρ = 880 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
v = ?p0​pp0​ − p = 1300 Pastagnation point

A pitot-static tube in a wind tunnel reads a difference of 1300 Pa between the stagnation pressure and the static pressure. The air density is 1.2 kg/m³. Find the air speed v.

p0 − p = 1300 Paρ = 1.2 kg/m³
v = m/s
4.Continuity & BernoulliHard
pair​ = 30 kPaQ = ?d = 20 mmh = 1 m

A closed water tank has compressed air above the water at a gauge pressure of 30 kPa. Water leaves through an opening with a diameter of 20 mm, 1 m below the water surface, into the open air. Ignoring losses, find the flow rate Q. Use g = 9.81 m/s².

pair = 30 kPa (gauge)h = 1 md = 20 mmρ = 1000 kg/m³g = 9.81 m/s²
Q = L/s
5.Pipe friction & head lossMedium
V = 1.5 m/sD = 100 mmL = 800 mf = 0.02

Water flows at a mean velocity of 1.5 m/s through a pipe 800 m long with an inside diameter of 100 mm. Use the Darcy friction factor f = 0.02 and g = 9.81 m/s². Find the friction head loss hf.

V = 1.5 m/sL = 800 mD = 100 mmf = 0.02g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 5free outletH = ?L = 150 m, D = 100 mm, f = 0.0153× bend (K = 0.3)

A pipe 150 m long with an inside diameter of 100 mm (Darcy friction factor f = 0.015) 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 20 L/s?

Q = 20 L/sL = 150 mD = 100 mmf = 0.015Kentrance = 0.5Kbend = 0.3 (×3)Kvalve = 5
H = m
7.Pumps & pump powerMedium
PQ = 50 L/sH = 70 m

A pump delivers 50 L/s of water (ρ = 1000 kg/m³) against a head of 70 m. The pump efficiency is 72% 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 = 50 L/sH = 70 mηpump = 72%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 15 L/sΔz = 5 mL = 400 m, D = 100 mm, f = 0.018, ΣK = 8

A pump moves 15 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 400 m long with an inside diameter of 100 mm and a Darcy friction factor f = 0.018; the minor-loss coefficients add up to ΣK = 8 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 82%. Find the shaft power Pshaft in kW.

Q = 15 L/sΔz = 5 mL = 400 mD = 100 mmf = 0.018ΣK = 8η = 82%
Pshaft = kW
9.Open-channel flow (Manning)Medium
b = 4.5 my = 1.2 mn = 0.022, S = 0.0008

A rectangular clean earth channel is 4.5 m wide. Water flows uniformly 1.2 m deep. Manning n = 0.022 and the bed slope is S = 0.0008. Find the flow rate Q in m³/s.

b = 4.5 my = 1.2 mn = 0.022S = 0.0008
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 2 my = 1.9 mn = 0.03, Q = 3.7 m³/s

A rectangular grass-lined earth channel 2 m wide must carry 3.7 m³/s in uniform flow at a depth of 1.9 m. Manning n = 0.03. Find the required bed slope S (in m/m).

Q = 3.7 m³/sb = 2 my = 1.9 mn = 0.03
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 55.18 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 = 3 + 1.5/2 = 3.75 m
A = H·b = 1.5·1 = 1.5 m²
gated = 3 mH = 1.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·3.75·1.5 = 55.18 kN

Answer

F = 55.18 kN
2.Hydrostatic force

Answer: ycp = 4.667 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 = 3 + 3/2 = 4.5 m
A = H·b = 3·2 = 6 m²
gated = 3 mH = 3 mF

Resultant force

F = ρ·g·yc·A = 880·9.81·4.5·6 = 233.1 kN

Centre of pressure

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

Ic = b·H³/12 = 2·3³/12 = 4.5 m⁴
ycp = yc + Ic/(yc·A) = 4.5 + 4.5/(4.5·6) = 4.667 m

Answer

ycp = 4.667 m
3.Continuity & Bernoulli

Answer: v = 46.55 m/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.

Bernoulli to the stagnation point

The flow comes to rest at the tip, so its kinetic energy shows up as extra pressure.

p0 − p = ½ρv²
v = √(2·1300/1.2) = 46.55 m/s

Answer

v = 46.55 m/s
4.Continuity & Bernoulli

Answer: Q = 2.803 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.

Bernoulli from the surface to the jet

v = √(2·(30000/1000 + 9.81·1)) = 8.923 m/s

Flow rate

Q = A·v = 0.0003142·8.923 = 0.002803 m³/s = 2.803 L/s

Answer

Q = 2.803 L/s
5.Pipe friction & head loss

Answer: hf = 18.35 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) = 1.5²/(2·9.81) = 0.1147 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.02·(800/0.1)·1.5²/(2·9.81) = 18.35 m

Answer

hf = 18.35 m
6.Pipe friction & head loss

Answer: H = 9.882 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 = 0.02/0.007854 = 2.546 m/s
V²/(2g) = 0.3305 m

Loss coefficients

f·L/D = 0.015·150/0.1 = 22.5
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 + 22.5 + 6.4)·0.3305 = 9.882 m

Answer

H = 9.882 m
7.Pumps & pump power

Answer: Pel = 50.2 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 = 1000·9.81·0.05·70 = 34.34 kW

Shaft power

Pshaft = 34.34/0.72 = 47.69 kW

Electrical power

Pel = 47.69/0.95 = 50.2 kW

Answer

Pel = 50.2 kW
8.Pumps & pump power

Answer: Pshaft = 3.566 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 = 0.015/0.007854 = 1.91 m/s
V²/(2g) = 0.1859 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (72 + 8)·0.1859 = 14.87 m

Pump head

H = Δz + hL = 5 + 14.87 = 19.87 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.015·19.87/0.82 = 3.566 kW

Answer

Pshaft = 3.566 kW
9.Open-channel flow (Manning)

Answer: Q = 5.896 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 = 4.5·1.2 = 5.4 m²
P = b + 2y = 4.5 + 2·1.2 = 6.9 m
R = A/P = 0.7826 m

Velocity

V = (1/0.022)·0.78262/3·0.00081/2 = 1.092 m/s

Flow rate

Q = A·V = 5.4·1.092 = 5.896 m³/s

Answer

Q = 5.896 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.001499 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·y = 2·1.9 = 3.8 m²
P = b + 2y = 2 + 2·1.9 = 5.8 m
R = A/P = 0.6552 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.03·3.7/(3.8·0.7543) = 0.03872
S = 0.03872² = 0.001499

Answer

S = 0.001499

That is a fall of 1.499 m per kilometre.

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