Fluid Mechanics: cram pack

Formula sheets, the key method steps for every topic and 8 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)

2Practice problems

1.Hydrostatic forceMedium
gated = 1.5 mH = 1.5 m

A vertical rectangular gate 1.5 m wide sits in the wall of a tank of water, with its top edge 1.5 m below the surface. Find the resultant hydrostatic force F on the gate.

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

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

d = 1 mH = 1 mb = 1 mρ = 1025 kg/m³g = 9.81 m/s²
F = kN
3.Continuity & BernoulliMedium
12d1​ = 150 mm, p1​ = 250 kPad2​ = 75 mm, p2​ = ?

Water flows through a horizontal pipe that narrows from 150 mm to 75 mm. In the wide section the pressure is 250 kPa and the velocity is 2.25 m/s. Ignoring losses, find the pressure p2 in the narrow section.

d1 = 150 mmd2 = 75 mmp1 = 250 kPav1 = 2.25 m/sρ = 1000 kg/m³
p2 = kPa
4.Continuity & BernoulliHard
C213 m5 md = 50 mmQ = ?

A hose with an inner diameter of 50 mm siphons water from an open tank. The highest point C of the hose is 3 m above the water surface, and the outlet (open to the air) is 5 m below the water surface. Ignore losses and take g = 9.81 m/s². Find the flow rate Q.

d = 50 mmzC = +3 mz2 = −5 mg = 9.81 m/s²
Q = L/s
5.Pipe friction & head lossMedium
V = 1.9 m/sD = 50 mmL = 400 mf = 0.022

Water (ρ = 1000 kg/m³) flows at 1.9 m/s through a horizontal pipe, 400 m long, with an inside diameter of 50 mm. Use the Darcy friction factor f = 0.022 and g = 9.81 m/s². Find the pressure drop Δp over the pipe in kPa.

V = 1.9 m/sL = 400 mD = 50 mmf = 0.022ρ = 1000 kg/m³
Δp = kPa
6.Pipe friction & head lossHard
K = 5Δz = 20 mL = 100 m, D = 300 mm, f = 0.024× bend (K = 0.3)

Two open reservoirs are joined by a pipe 100 m long with an inside diameter of 300 mm and a Darcy friction factor f = 0.02. The water surface of the upper reservoir is 20 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 = 5) 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 = 20 mL = 100 mD = 300 mmf = 0.02Kentrance = 0.5Kbend = 0.3 (×4)Kvalve = 5Kexit = 1.0
Q = L/s
7.Pumps & pump powerMedium
PQ = 15 L/sH = 16 m

In a test, a pump delivers 15 L/s of water (ρ = 1000 kg/m³) against a head of 16 m while its shaft takes 3 kW. Use g = 9.81 m/s². Find the pump efficiency η in percent.

Q = 15 L/sH = 16 mPshaft = 3 kWg = 9.81 m/s²
η = %
8.Pumps & pump powerHard
PQ = 80 L/sΔz = 10 mL = 500 m, D = 250 mm, f = 0.015, ΣK = 6

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 10 m higher. The pipe is 500 m long with an inside diameter of 250 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 78%. Find the shaft power Pshaft in kW.

Q = 80 L/sΔz = 10 mL = 500 mD = 250 mmf = 0.015ΣK = 6η = 78%
Pshaft = kW

3Solutions

1.Hydrostatic force

Answer: F = 49.66 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 = 1.5 + 1.5/2 = 2.25 m
A = H·b = 1.5·1.5 = 2.25 m²
gated = 1.5 mH = 1.5 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·2.25·2.25 = 49.66 kN

Answer

F = 49.66 kN
2.Hydrostatic force

Answer: F = 15.08 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 = 1·1 = 1 m²
gated = 1 mH = 1 mF

Resultant force

F = ρ·g·yc·A = 1025·9.81·1.5·1 = 15.08 kN

Answer

F = 15.08 kN
3.Continuity & Bernoulli

Answer: p2 = 212 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 = 2.25·(150/75)² = 9 m/s
½ρ(v1² − v2²) = ½·1000·(2.25² − 9²)/1000 = −37.97 kPa
p2 = p1 + ½ρ(v1² − v2²) = 250 + (−37.97) = 212 kPa

Answer

p2 = 212 kPa
4.Continuity & Bernoulli

Answer: Q = 19.45 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.

Velocity in the hose

Surface and outlet are both open to the air, so the pressure terms cancel.

v = √(2g·5) = √(2·9.81·5) = 9.905 m/s

Flow rate

Q = A·v = 0.001963·9.905 = 0.01945 m³/s = 19.45 L/s

Answer

Q = 19.45 L/s
5.Pipe friction & head loss

Answer: Δp = 317.7 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) = 0.022·(400/0.05)·1.9²/(2·9.81) = 32.38 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 = 1000·9.81·32.38 = 317680 Pa = 317.7 kPa

Answer

Δp = 317.7 kPa
6.Pipe friction & head loss

Answer: Q = 369.4 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 = 0.02·100/0.3 = 6.667
ΣK = 0.5 + 4·0.3 + 5 + 1.0 = 7.7

Energy equation

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

20 = (6.667 + 7.7)·V²/(2·9.81)
V = √(2·9.81·20/14.37) = 5.226 m/s

Flow rate

Q = V·π·D²/4 = 5.226·0.07069 = 0.3694 m³/s = 369.4 L/s

Answer

Q = 369.4 L/s
7.Pumps & pump power

Answer: η = 78.48 %

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 = 1000·9.81·0.015·16 = 2.354 kW

Efficiency

η = Ph/Pshaft = 2.354/3 = 78.48%

Answer

η = 78.48%
8.Pumps & pump power

Answer: Pshaft = 14.97 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 = 0.08/0.04909 = 1.63 m/s
V²/(2g) = 0.1354 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (30 + 6)·0.1354 = 4.874 m

Pump head

H = Δz + hL = 10 + 4.874 = 14.87 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.08·14.87/0.78 = 14.97 kW

Answer

Pshaft = 14.97 kW

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