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 = 2 mH = 2 m

A vertical rectangular gate 2 m wide sits in the wall of a tank of water, with its top edge 2 m below the surface. Find the resultant hydrostatic force F on the gate.

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

A vertical rectangular gate 1.5 m wide sits in the wall of a tank of glycerin, with its top edge 1 m below the surface. Find the depth ycp of the centre of pressure below the surface.

d = 1 mH = 2.5 mb = 1.5 mρ = 1260 kg/m³g = 9.81 m/s²
ycp = m
3.Continuity & BernoulliMedium
v = ?p0​pp0​ − p = 400 Pastagnation point

A pitot-static tube in a wind tunnel reads a difference of 400 Pa between the stagnation pressure and the static pressure. The air density is 1.2 kg/m³. Find the air speed v.

p0 − p = 400 Paρ = 1.2 kg/m³
v = m/s
4.Continuity & BernoulliHard
12d1​ = 150 mm, p1​ = 370 kPad2​ = 100 mm, p2​ = ?Δz = 10 m

Water flows up through a pipe that narrows from 150 mm to 100 mm while rising 10 m. At section 1 the pressure is 370 kPa and the velocity is 2.75 m/s. Ignoring losses, find the pressure p2 at section 2.

d1 = 150 mmd2 = 100 mmp1 = 370 kPav1 = 2.75 m/sΔz = 10 mρ = 1000 kg/m³
p2 = kPa
5.Pipe friction & head lossMedium
V = 1.8 m/sD = 300 mmL = 300 mf = 0.02

Water flows at a mean velocity of 1.8 m/s through a pipe 300 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.

V = 1.8 m/sL = 300 mD = 300 mmf = 0.02g = 9.81 m/s²
hf = m
6.Pipe friction & head lossHard
K = 5Δz = ?L = 200 m, D = 200 mm, f = 0.0184× bend (K = 0.3)

Two open reservoirs are joined by a pipe 200 m long with an inside diameter of 200 mm and a Darcy friction factor f = 0.018. 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 100 L/s?

Q = 100 L/sL = 200 mD = 200 mmf = 0.018Kentrance = 0.5Kbend = 0.3 (×4)Kvalve = 5Kexit = 1.0
Δz = m
7.Pumps & pump powerMedium
PQ = 40 L/sH = 72 m

A pump delivers 40 L/s of water (ρ = 1000 kg/m³) against a head of 72 m. The pump efficiency is 78% 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 = 40 L/sH = 72 mηpump = 78%ηmotor = 95%g = 9.81 m/s²
Pel = kW
8.Pumps & pump powerHard
PQ = 120 L/sΔz = 34 mL = 300 m, D = 250 mm, f = 0.025, ΣK = 8

A pump moves 120 L/s of water (ρ = 1000 kg/m³) from an open lower reservoir to an upper tank whose water surface is 34 m higher. The pipe is 300 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 = 8 (entrance and exit included). Use g = 9.81 m/s². The pump efficiency is 72%. Find the shaft power Pshaft in kW.

Q = 120 L/sΔz = 34 mL = 300 mD = 250 mmf = 0.025ΣK = 8η = 72%
Pshaft = kW

3Solutions

1.Hydrostatic force

Answer: F = 117.7 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 + 2/2 = 3 m
A = H·b = 2·2 = 4 m²
gated = 2 mH = 2 mF

Resultant force

F = ρ·g·yc·A = 1000·9.81·3·4 = 117.7 kN

Answer

F = 117.7 kN
2.Hydrostatic force

Answer: ycp = 2.481 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 + 2.5/2 = 2.25 m
A = H·b = 2.5·1.5 = 3.75 m²
gated = 1 mH = 2.5 mF

Resultant force

F = ρ·g·yc·A = 1260·9.81·2.25·3.75 = 104.3 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) = 2.25 + 1.953/(2.25·3.75) = 2.481 m

Answer

ycp = 2.481 m
3.Continuity & Bernoulli

Answer: v = 25.82 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 = √(2·400/1.2) = 25.82 m/s

Answer

v = 25.82 m/s
4.Continuity & Bernoulli

Answer: p2 = 256.5 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 = 2.75·(150/100)² = 6.188 m/s
½ρ(v1² − v2²) = ½·1000·(2.75² − 6.188²)/1000 = −15.36 kPa
ρgΔz = 1000·9.81·10/1000 = 98.1 kPa
p2 = p1 + ½ρ(v1² − v2²) − ρgΔz = 370 + (−15.36) − 98.1 = 256.5 kPa

Answer

p2 = 256.5 kPa
5.Pipe friction & head loss

Answer: hf = 3.303 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) = 1.8²/(2·9.81) = 0.1651 m

Darcy–Weisbach

hf = f·(L/D)·V²/(2g) = 0.02·(300/0.3)·1.8²/(2·9.81) = 3.303 m

Answer

hf = 3.303 m
6.Pipe friction & head loss

Answer: Δz = 13.27 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 = 0.1/0.03142 = 3.183 m/s
V²/(2g) = 0.5164 m

Loss coefficients

f·L/D = 0.018·200/0.2 = 18
ΣK = 0.5 + 4·0.3 + 5 + 1.0 = 7.7

Total head loss

hf = 18·0.5164 = 9.296 m
hm = 7.7·0.5164 = 3.976 m
Δz = hf + hm = 13.27 m

Answer

Δz = 13.27 m
7.Pumps & pump power

Answer: Pel = 38.13 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 = 1000·9.81·0.04·72 = 28.25 kW

Shaft power

Pshaft = 28.25/0.78 = 36.22 kW

Electrical power

Pel = 36.22/0.95 = 38.13 kW

Answer

Pel = 38.13 kW
8.Pumps & pump power

Answer: Pshaft = 74.51 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 = 0.12/0.04909 = 2.445 m/s
V²/(2g) = 0.3046 m

Head losses

hL = (f·L/D + ΣK)·V²/(2g) = (30 + 8)·0.3046 = 11.57 m

Pump head

H = Δz + hL = 34 + 11.57 = 45.57 m

Shaft power

Pshaft = ρ·g·Q·H/η = 1000·9.81·0.12·45.57/0.72 = 74.51 kW

Answer

Pshaft = 74.51 kW

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