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

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

d = 3 mH = 3 mb = 3 mρ = 1025 kg/m³g = 9.81 m/s²
F = kN
3.Continuity & BernoulliMedium
v = ?p0​pp0​ − p = 6 kPastagnation point

A pitot-static tube in a water pipe reads a difference of 6 kPa between the stagnation pressure and the static pressure. Find the water velocity v at the tip.

p0 − p = 6 kPaρ = 1000 kg/m³
v = m/s
4.Continuity & BernoulliHard
12d1​ = 100 mm, p1​ = 330 kPad2​ = 50 mm, p2​ = ?Δz = 6 m

Water flows up through a pipe that narrows from 100 mm to 50 mm while rising 6 m. At section 1 the pressure is 330 kPa and the velocity is 0.5 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 100 mmd2 = 50 mmp1 = 330 kPav1 = 0.5 m/sΔz = 6 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
Q = 150 L/sD = 300 mmL = 500 mf = 0.02

Water flows at 150 L/s through a pipe 500 m long with an inside diameter of 300 mm. Use the Darcy friction factor f = 0.02 and g = 9.81 m/s². Find the friction head loss hf.

Q = 150 L/sL = 500 mD = 300 mmf = 0.02g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 2Δz = 25 mL = 200 m, D = 300 mm, f = 0.0184× bend (K = 0.3)

Two open reservoirs are joined by a pipe 200 m long with an inside diameter of 300 mm and a Darcy friction factor f = 0.018. The water surface of the upper reservoir is 25 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 = 2) 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 = 25 mL = 200 mD = 300 mmf = 0.018Kentrance = 0.5Kbend = 0.3 (×4)Kvalve = 2Kexit = 1.0
Q = L/s
7.Pumps & pump powerMedium
PQ = 60 L/sH = 54 m

In a test, a pump delivers 60 L/s of water (ρ = 1000 kg/m³) against a head of 54 m while its shaft takes 53 kW. Use g = 9.81 m/s². Find the pump efficiency η in percent.

Q = 60 L/sH = 54 mPshaft = 53 kWg = 9.81 m/s²
η = %
8.Pumps & pump powerHard
PQ = 80 L/sΔz = 5 mL = 150 m, D = 250 mm, f = 0.025, ΣK = 5

A pump moves 80 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 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 = 5 (entrance and exit included). Use g = 9.81 m/s². Find the head H the pump must add.

Q = 80 L/sΔz = 5 mL = 150 mD = 250 mmf = 0.025ΣK = 5
H = m
9.Open-channel flow (Manning)Medium
b = 1 my = 2.2 mn = 0.012, S = 0.0015

A rectangular finished concrete channel is 1 m wide. Water flows uniformly 2.2 m deep. Manning n = 0.012 and the bed slope is S = 0.0015. Find the flow rate Q in m³/s.

b = 1 my = 2.2 mn = 0.012S = 0.0015
Q = m³/s
10.Open-channel flow (Manning)Hard
b = 2 my = 2.3 mn = 0.03, Q = 5.4 m³/s

A rectangular grass-lined earth channel 2 m wide must carry 5.4 m³/s in uniform flow at a depth of 2.3 m. Manning n = 0.03. Find the required bed slope S (in m/m).

Q = 5.4 m³/sb = 2 my = 2.3 mn = 0.03
S = m/m

3Solutions

1.Hydrostatic force

Answer: F = 193.1 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 = 2.5·1.5 = 3.75 m²
gated = 4 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·5.25·3.75 = 193.1 kN

Answer

F = 193.1 kN
2.Hydrostatic force

Answer: F = 407.2 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 + 3/2 = 4.5 m
A = H·b = 3·3 = 9 m²
gated = 3 mH = 3 mF

Resultant force

F = ρ·g·yc·A = 1025·9.81·4.5·9 = 407.2 kN

Answer

F = 407.2 kN
3.Continuity & Bernoulli

Answer: v = 3.464 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 = √(2·6000/1000) = 3.464 m/s

Answer

v = 3.464 m/s
4.Continuity & Bernoulli

Answer: p2 = 269.3 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 = 0.5·(100/50)² = 2 m/s
½ρ(v1² − v2²) = ½·1000·(0.5² − 2²)/1000 = −1.875 kPa
ρgΔz = 1000·9.81·6/1000 = 58.86 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 330 + (−1.875) − 58.86 = 269.3 kPa

Answer

p2 = 269.3 kPa
5.Pipe friction & head loss

Answer: hf = 7.651 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 = 0.15/0.07069 = 2.122 m/s

Velocity head

V²/(2g) = 2.122²/(2·9.81) = 0.2295 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.02·(500/0.3)·2.122²/(2·9.81) = 7.651 m

Answer

hf = 7.651 m
6.Pipe friction & head loss

Answer: Q = 383.1 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 = 0.018·200/0.3 = 12
ΣK = 0.5 + 4·0.3 + 2 + 1.0 = 4.7

Energy equation

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

25 = (12 + 4.7)·V²/(2·9.81)
V = √(2·9.81·25/16.7) = 5.42 m/s

Flow rate

Q = V·π·D²/4 = 5.42·0.07069 = 0.3831 m³/s = 383.1 L/s

Answer

Q = 383.1 L/s
7.Pumps & pump power

Answer: η = 59.97 %

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 = 1000·9.81·0.06·54 = 31.78 kW

Efficiency

η = Ph/Pshaft = 31.78/53 = 59.97%

Answer

η = 59.97%
8.Pumps & pump power

Answer: H = 7.708 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 = 0.08/0.04909 = 1.63 m/s
V²/(2g) = 0.1354 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (15 + 5)·0.1354 = 2.708 m

Pump head

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

H = Δz + hL = 5 + 2.708 = 7.708 m

Answer

H = 7.708 m
9.Open-channel flow (Manning)

Answer: Q = 3.902 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 = 1·2.2 = 2.2 m²
P = b + 2y = 1 + 2·2.2 = 5.4 m
R = A/P = 0.4074 m

Velocity

V = (1/0.012)·0.40742/3·0.00151/2 = 1.774 m/s

Flow rate

Q = A·V = 2.2·1.774 = 3.902 m³/s

Answer

Q = 3.902 m³/s
10.Open-channel flow (Manning)

Answer: S = 0.002007 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 = 2·2.3 = 4.6 m²
P = b + 2y = 2 + 2·2.3 = 6.6 m
R = A/P = 0.697 m

Solve Manning for S

S1/2 = n·Q/(A·R2/3) = 0.03·5.4/(4.6·0.7861) = 0.0448
S = 0.0448² = 0.002007

Answer

S = 0.002007

That is a fall of 2.007 m per kilometre.

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