Chapter 14 Q&A — Fluids
Question 1: Pressure and Why It Matters in Fluids
Q: Why is pressure such a central concept in fluid mechanics, and how does it differ fundamentally from forces in solid mechanics?
A: Pressure (P = F/A) is central to fluids because fluids flow—they cannot support shear stress the way solids can. In a solid, you can push on one side without affecting the opposite side much. In a fluid, a small push creates pressure that spreads everywhere at constant volume: pushing on one end of a fluid in a container increases pressure uniformly throughout.
Key differences from solid mechanics:
- Fluids have no preferred orientation—pressure acts equally in all directions (isotropic)
- Fluid elements can move past each other without resistance (ignoring viscosity)
- Pressure is the only "normal force" that matters in static fluids
Physical basis: Pressure arises from collisions of fluid molecules with surfaces. In a gas, this is direct—air molecules bounce off walls, creating pressure. In a liquid, molecules are packed densely; pressure is the result of cohesive forces transmitted through the liquid. Deeper in the fluid, more weight presses down, so pressure increases with depth.
Practical consequence: A small hole in a dam at depth creates danger because pressure is high. A hole near the surface is harmless. The same hole, same size, but pressure difference (ΔP = ρgh) can be enormous—this is why dams are thicker at the bottom.
Question 2: Archimedes' Principle and Why Objects Float or Sink
Q: State Archimedes' principle rigorously and explain the physical mechanism behind it. Why do some objects float and others sink?
A: Archimedes' Principle: The buoyant force on any object immersed in (or floating on) a fluid equals the weight of the fluid displaced: \[ F_b = \rho_{fluid} \cdot g \cdot V_{displaced} \]
Physical Mechanism: Pressure increases with depth (P = P₀ + ρgh). Consider a cube of fluid surrounded by more fluid. The pressure on the bottom is higher than on the top. This pressure difference creates an upward force. If you replace that fluid cube with a solid object, the same pressure difference acts on it—pushing it upward. The magnitude equals exactly the weight of the fluid that was there, which is why F_b = ρ_fluid × g × V_displaced.
Floating vs. Sinking:
The condition depends on comparing the average density of the object to the fluid:
-
Float: ρ_object < ρ_fluid (object lighter per unit volume than fluid)
- At equilibrium, the object settles until buoyant force = weight
- Only part of the object submerges; the rest sticks above the surface
- Example: wood (≈600 kg/m³) in water (1000 kg/m³)
-
Sink: ρ_object > ρ_fluid (object denser than fluid)
- Buoyant force never equals weight; the object sinks to the bottom
- Example: iron (≈7800 kg/m³) in water
-
Neutral buoyancy: ρ_object = ρ_fluid
- Buoyant force exactly equals weight at any depth
- Object neither sinks nor floats; it's "weightless" in the fluid
- Example: submarines adjust buoyancy by taking on/expelling water
Real-world nuance: A ship made of steel (7800 kg/m³) floats because its average density (steel + air cavity inside) is less than water. Fill the cavity with water (sink it), and ρ_avg > ρ_water—it sinks.
Question 3: Continuity Equation and Mass Conservation in Flowing Fluids
Q: Derive the continuity equation and explain why water flows faster through a narrow nozzle. What assumptions are required?
A: The Continuity Equation: \[ A_1 v_1 = A_2 v_2 \]
or more generally: \[ \frac{dV}{dt} = A \cdot v = \text{constant} \]
where V is volume, A is cross-sectional area, v is flow speed, and the right side is the volume flow rate.
Derivation via Mass Conservation:
In a flowing fluid (incompressible), mass must be conserved. Consider a pipe section: in time Δt, a fluid element at location 1 (area A₁, speed v₁) travels distance v₁Δt and sweeps volume A₁v₁Δt. At location 2 (narrower, area A₂), the same mass flows through in the same time, sweeping volume A₂v₂Δt.
For incompressible flow (constant density ρ): \[ \rho A_1 v_1 \Delta t = \rho A_2 v_2 \Delta t \] \[ A_1 v_1 = A_2 v_2 \]
Physical Interpretation:
- Water cannot pile up or disappear in the pipe
- As the pipe narrows (A decreases), flow speed must increase (v increases) to maintain the same volume flow rate
- Narrower nozzle = faster water
Real example: A garden hose flows at ~2 m/s in the hose (large area, slow flow). Attach a narrow nozzle, and water shoots out at ~10 m/s. The pressure is the same; the nozzle forces the water to speed up.
Required Assumptions:
- Incompressible flow — density ρ is constant (good for liquids; gases only under limited conditions)
- Steady flow — flow properties don't change with time (not valid for waves, turbulence in some cases)
- No mass added or removed — no pumps or drains between locations 1 and 2
Question 4: Bernoulli's Principle and Why Faster Fluids Have Lower Pressure
Q: Derive Bernoulli's equation from energy conservation. Why does pressure drop when fluid speed increases, and how does this explain aircraft lift?
A: Bernoulli's Equation: \[ P + \frac{1}{2}\rho v^2 + \rho g h = \text{constant along a streamline} \]
Derivation via Energy Conservation:
Consider a small fluid element moving along a streamline from point 1 to point 2. The work-energy theorem states: \[ \text{Work by all forces} = \Delta KE \]
Forces acting:
- Pressure forces: W_P = (P₁ − P₂) × Volume
- Gravitational force: W_g = −ρgΔh × Volume (negative if height increases)
Energy equation: \[ (P_1 - P_2)V + (-\rho g \Delta h V) = \frac{1}{2}\rho V (v_2^2 - v_1^2) \]
Dividing by V: \[ P_1 - P_2 - \rho g (h_2 - h_1) = \frac{1}{2}\rho(v_2^2 - v_1^2) \]
Rearranging: \[ P_1 + \frac{1}{2}\rho v_1^2 + \rho g h_1 = P_2 + \frac{1}{2}\rho v_2^2 + \rho g h_2 \]
This is Bernoulli's equation—each term is energy density (energy per unit volume):
- P = pressure energy density
- ½ρv² = kinetic energy density
- ρgh = gravitational potential energy density
Why Fast Flow Has Low Pressure:
In Bernoulli's equation, the sum is constant. If speed v increases (kinetic energy density ↑), then P must decrease to keep the sum constant. This is not coincidence; it follows from energy conservation:
- Fluid moves faster when it's in a region of lower pressure
- The pressure does less work, leaving more energy for kinetic motion
- In a narrowing pipe: continuity forces speed ↑ → Bernoulli forces pressure ↓
Aircraft Lift (Bernoulli Explanation):
An aircraft wing is curved: the upper surface is more curved than the lower surface.
- Air flows faster over the upper surface (due to streamline geometry)
- By Bernoulli, fast air = low pressure
- Pressure on upper surface < pressure on lower surface
- Net upward force = (P_bottom − P_top) × Wing Area = LIFT
This works at any airspeed: faster planes have higher pressure differences and more lift. This is the foundation of aerodynamic wing design.
Question 5: Viscosity, Stokes Drag, and Terminal Velocity
Q: Define viscosity microscopically. Derive Stokes drag force. Why do small falling objects reach terminal velocity so quickly?
A: Viscosity — Microscopic Picture:
Viscosity η arises from intermolecular cohesive forces. When adjacent layers of fluid move at different speeds, fast-moving molecules collide with slow-moving molecules, transferring momentum. This internal "friction" resists flow.
Viscosity coefficients:
- Water at 20°C: η ≈ 0.001 Pa·s (thin)
- Honey at 20°C: η ≈ 2–10 Pa·s (thick)
- Air at 20°C: η ≈ 0.00002 Pa·s (very thin)
Temperature effects:
- Liquids: heating increases molecular motion, weakens intermolecular bonds → η decreases (honey thins when heated)
- Gases: heating increases molecular speed → more momentum transfer → η increases (counterintuitive but true)
Stokes Drag Force:
For a sphere of radius r moving at speed v through a viscous fluid with viscosity η: \[ F_d = 6\pi \eta r v \]
This formula applies in the Stokes regime (low Reynolds number, Re < 1):
- Drag is proportional to v (not v², as in high-speed aerodynamic drag)
- Drag is proportional to object size r and fluid viscosity η
- Doubling velocity doubles drag; doubling radius doubles drag
Terminal Velocity:
A falling object experiences:
- Gravitational force (downward): F_g = mg
- Drag force (upward): F_d = 6πηrv
- Buoyant force (upward): F_b = ρ_fluid g V
At terminal velocity, net force = 0: \[ mg = F_d + F_b \] \[ mg = 6\pi\eta r v_{terminal} + \rho_{fluid} g V \]
For small objects or high-viscosity fluids, Stokes drag dominates, so: \[ mg \approx 6\pi\eta r v_{terminal} \] \[ v_{terminal} \approx \frac{mg}{6\pi\eta r} \]
Why Small Objects Reach Terminal Velocity Quickly:
Acceleration: \( a = g - \frac{F_d}{m} = g - \frac{6\pi\eta r v}{m} \)
For small objects (small m, small r), the ratio \( \frac{\eta r}{m} \) is large. Drag force grows quickly with v, and terminal velocity is reached in milliseconds.
Example: A raindrop (r ≈ 1 mm, m ≈ 0.01 g) reaches terminal velocity (~10 m/s) in ~1 second. A bowling ball (r ≈ 0.1 m, m ≈ 7 kg) takes much longer to reach its (higher) terminal velocity because inertia dominates.
Question 6: Reynolds Number and the Laminar-to-Turbulent Transition
Q: Define the Reynolds number and explain why the transition from laminar to turbulent flow occurs at a critical Re value. How does this affect pipe flow?
A: Reynolds Number Definition: \[ Re = \frac{\rho v D}{\eta} \]
where:
- ρ = fluid density (kg/m³)
- v = average flow velocity (m/s)
- D = characteristic length scale (pipe diameter, object size)
- η = dynamic viscosity (Pa·s)
Re is dimensionless—it compares inertial forces (ρv²) to viscous forces (ηv/D).
Physical Interpretation:
- Re << 1: Viscous forces dominate; fluid creeps slowly. Example: honey pouring.
- Re ~ 1–100: Mixed regime; viscosity still important but inertia growing.
- Re >> 1: Inertial forces dominate; viscosity is negligible. Example: water flowing in a river.
Laminar vs. Turbulent Flow:
Laminar flow (Re < 2300 in pipes):
- Fluid moves in parallel layers
- No mixing between layers (except by molecular diffusion)
- Pressure drop ∝ v (proportional to flow speed)
- Energy efficient; steady and predictable
Turbulent flow (Re > 4000 in pipes):
- Chaotic eddies and vortices; rapid mixing
- Flow is noisy and chaotic on small scales
- Pressure drop ∝ v² (quadratic; much more energy required)
- More drag; higher energy cost to pump
Transition region (2300 < Re < 4000):
- Neither fully laminar nor turbulent
- Instabilities appear; flow oscillates between regimes
Critical Re Value: The transition occurs when inertial forces grow strong enough to overcome viscous damping. Small perturbations (turbulence seeds) grow exponentially rather than decay. Experiments confirm:
- Smooth straight pipes: Critical Re ≈ 2300
- Rough pipes or elbows: Critical Re lower (~500–1000) because surface roughness seeds disturbances
Practical Consequences:
- Water in household pipes (v ~ 1 m/s, D ~ 0.02 m, η ~ 0.001 Pa·s): Re = (1000 × 1 × 0.02) / 0.001 ≈ 20,000 → turbulent. You hear water rushing; energy is wasted heating the pipe.
- Oil in a narrow tube (lower v, higher η): Re could be < 1 → laminar. Oil creeps slowly without turbulence.
- Aircraft wing (v ~ 100 m/s, D ~ 2 m, air η ~ 0.00002 Pa·s): Re = (1.2 × 100 × 2) / 0.00002 ≈ 12 million → turbulent. Boundary layer turbulent; drag calculated from empirical drag coefficients, not Stokes law.
Question 7: Pressure Measurement and Manometers
Q: How do manometers work? Derive the relationship between pressure difference and height difference in a U-tube manometer.
A: Manometer Principle:
A manometer is a tube filled with fluid (usually mercury or water) in a U-shape. One end connects to the system whose pressure you want to measure; the other end is open to atmosphere (or closed).
Derivation for Open Manometer:
Let P_x = unknown pressure in the system, P_atm = atmospheric pressure.
At the same horizontal level inside the fluid (at the bottom of the U-tube, or at any horizontal line): \[ P_x + \rho_{fluid} g h_1 = P_{atm} + \rho_{fluid} g h_2 \]
where h₁ and h₂ are heights of fluid on the system side and atmosphere side.
If the fluid column on the system side is lower by Δh = h₂ − h₁: \[ P_x + \rho_{fluid} g (h_2 - \Delta h) = P_{atm} + \rho_{fluid} g h_2 \] \[ P_x = P_{atm} + \rho_{fluid} g \Delta h \]
If the system pressure is lower than atmospheric (P_x < P_atm), the mercury is sucked up on the system side, so: \[ P_{atm} - P_x = \rho_{fluid} g \Delta h \] \[ \Delta h = \frac{P_{atm} - P_x}{\rho_{fluid} g} \]
Example with Mercury: If atmospheric pressure pushes a mercury column up by Δh = 0.76 m (760 mm): \[ P_{atm} = \rho_{Hg} g \Delta h = 13600 \times 10 \times 0.76 ≈ 103,360 \text{ Pa} ≈ 1 \text{ atm} \]
(This is the basis of the barometer: a sealed tube of mercury held up by atmospheric pressure.)
Advantages of manometers:
- Simple, no electronics
- Direct visual reading
- Sensitive (small pressure differences cause large column height changes)
Disadvantage:
- Slow response; fluid oscillates before settling
- Mercury is toxic (restricted in modern labs; water manometers used instead)
Question 8: Bernoulli Beyond Horizontal Pipes — Venturi Tube and Spray Bottle
Q: How do Venturi tubes and spray bottles use Bernoulli's principle to function? Derive the speed in the throat and pressure drop.
A: Venturi Tube (Differential Pressure Flowmeter):
A Venturi is a pipe that narrows and widens. As fluid passes through the narrow "throat," it speeds up (continuity) and pressure drops (Bernoulli). The pressure difference is proportional to the flow rate.
Setup:
- Wide section: diameter D₁, area A₁, pressure P₁, speed v₁
- Narrow section (throat): diameter D₂ < D₁, area A₂, pressure P₂, speed v₂
Step 1: Apply Continuity (mass conservation) \[ A_1 v_1 = A_2 v_2 \] \[ v_2 = v_1 \frac{A_1}{A_2} = v_1 \frac{D_1^2}{D_2^2} \]
Step 2: Apply Bernoulli (neglecting height change) \[ P_1 + \frac{1}{2}\rho v_1^2 = P_2 + \frac{1}{2}\rho v_2^2 \] \[ P_1 - P_2 = \frac{1}{2}\rho (v_2^2 - v_1^2) \]
Step 3: Substitute v₂ from continuity \[ \Delta P = P_1 - P_2 = \frac{1}{2}\rho v_1^2 \left[\left(\frac{D_1}{D_2}\right)^4 - 1\right] \]
For a 4:1 diameter ratio (D₁/D₂ = 4), the factor (4⁴ − 1) = 255: \[ \Delta P ≈ 127 \times \rho v_1^2 \]
A small inlet flow speed creates a huge pressure drop at the throat!
Real Application: Spray Bottle A spray bottle works by:
- Squeeze the trigger, forcing air through a narrow nozzle
- High-speed air (Bernoulli) creates low pressure
- Atmospheric pressure pushes liquid up the tube
- Low-pressure jet atomizes the liquid into a fine mist
Question 9: Drag Forces at High Speed vs. Low Speed
Q: Why does the drag force on a fast-moving object (like a car) scale as v², while slow objects (like a falling raindrop) experience drag ∝ v? When does each regime apply?
A: Low-Speed Regime: Stokes Drag (v-dependence)
\[ F_d = 6\pi\eta r v \]
Applies when Re << 1 (viscous forces dominate).
Examples:
- Raindrops falling: Re ~ 10–100 (small, low speed)
- Red blood cells in arteries: Re ~ 0.001 (tiny, blood viscosity high)
- Bacteria swimming: Re ~ 0.001 (microscopic)
Physical reason: At low Re, viscosity dominates. The object creates a viscous boundary layer around itself, and the drag arises from molecular friction between the object and fluid. Doubling velocity doubles momentum transfer → doubles drag.
High-Speed Regime: Quadratic Drag (v²-dependence)
\[ F_d = \frac{1}{2}\rho v^2 A C_d \]
where A = reference area, C_d = drag coefficient (dimensionless, depends on object shape).
Applies when Re >> 1 (inertial forces dominate).
Examples:
- Cars on highways: Re ~ 10⁶–10⁷ (large, high speed)
- Aircraft: Re ~ 10⁷–10⁸ (large, very high speed)
- Skydivers: Re ~ 10⁵–10⁶ (terminal velocity ~60 m/s)
Physical reason: At high Re, the object must continually accelerate fluid out of its way (creating a wake). Doubling velocity doubles the mass flow rate (ρAv) and doubles the momentum change per unit time (mv) → quadruples force. This is inertial drag, not viscous drag.
Transition Region:
Between Re ~ 100 and Re ~ 1000, the scaling transitions from linear to quadratic. Formulas become empirical. C_d often increases with Re in this range.
Terminal Velocity Comparison:
Low Re (Stokes): \( v_{terminal} \propto 1/r \) (smaller objects fall slower) High Re (quadratic): \( v_{terminal} \propto \sqrt{W/(ρ C_d A)} \) ∝ \( \sqrt{m} \) (bigger objects fall faster)
A dust particle reaches ~cm/s terminal velocity in air. A steel ball bearing reaches ~10 m/s. An elephant would reach higher speeds if dropped, but isn't normally dropped!
Question 10: Real-World Application — Why Submarines Must Be Built Differently Than Ships
Q: Use pressure concepts to explain why submarines have a much more restricted depth capability than ships, and what design changes are necessary.
A: Pressure with Depth: \[ P = P_0 + \rho g h \]
At sea level (h = 0), P = P₀ ≈ 101,325 Pa. In water:
- At h = 10 m: P = 101,325 + (1000)(10)(10) = 201,325 Pa (2 atm)
- At h = 100 m: P ≈ 1.1 MPa (11 atm)
- At h = 1000 m: P ≈ 10.1 MPa (100 atm)
- At h = 6000 m: P ≈ 60 MPa (600 atm)
Ship Design: Ships float on the surface. Interior pressure ≈ 1 atm (sea level). The hull only experiences pressure from outside water at the waterline; most of the ship is above water. Pressures are manageable: aluminum or steel hulls withstand this easily.
Submarine Design: Submarines operate completely submerged. The interior must maintain life-support pressures (1 atm); the exterior experiences full water pressure. The hull must withstand enormous pressure differentials.
Critical Design Constraints:
-
Material Strength:
- Steel yield strength: ~250–400 MPa
- At 1000 m depth (P ~ 10 MPa), a cylindrical hull must be designed for circumferential stress: \( \sigma = \frac{Pr}{t} \) where r = radius, t = wall thickness
- Rearranging: \( t = \frac{Pr}{\sigma} = \frac{(10 × 10^6)(5)}{(300 × 10^6)} ≈ 0.17 \) m (17 cm wall!)
- At 6000 m: t ~ 1 m walls needed for same radius (impractical)
-
Design Trade-offs:
- Nuclear subs: US Navy limit ~500–650 m (though classified military subs rumored deeper)
- Deep-diving research vessels (Alvin, Trieste): ~4000–11,000 m (tiny, heavily reinforced)
- Commercial submarines: rarely exceed 300 m
-
Fail-safe Design:
- Spherical or cylindrical pressure hull (optimal stress distribution)
- Single or double hull; external ballast tanks separate from crew compartment
- Emergency blow system to jettison water and surface rapidly
- Escape hatches for crew (if pressure hull ruptures, only that section floods)
-
Depth Record:
- James Cameron's Deepsea Challenger (2012): 10,994 m (Mariana Trench)
- Unique design: titanium sphere (small internal volume, minimizes stress)
- Could only accommodate one or two people
- Regular submarine operations: 200–500 m maximum
Conclusion: Pressure increases linearly with depth. Submarine hulls must resist pressures growing from ~0.1 MPa at 10 m to ~100 MPa at 1 km. This drives wall thickness, weight, and cost upward. Practical submarines are limited to ~500–1000 m by material science; only specialized deep-research vehicles reach greater depths, and only with extreme design compromises and minimal payload.
Ships float, so they avoid the problem. Submarines descend into it—this is why submarine engineering is one of the most demanding fields in mechanical engineering.
Have a question? 🤔
If something isn't clear or you have a question, ask it here. The answer will be published on this page.
