Fluids
8. Fluids — AP PHYSICS 1 Revision Notes & Topical Questions
5 min read 7 parts Lesson 1 of 14 2 quizzes
Lesson summary
8. Fluids — AP PHYSICS 1 notes: Calculate density and pressure, apply Pascal's principle and buoyancy, and use continuity and Bernoulli's equation to analyse fluid flow.Density — ρ = m/V, the mass per unit volume, in kg/m3.Example — a block 0.20 m × 0.10 m × 0.050 m of mass 2.7 k…
- Temperature
- Smaller area
- Pressure at depth
- Mercury barometer
- Buoyant force
- Vdisplaced
Section 1 of 7Density
Density
- ρ = m/V, the mass per unit volume, in kg/m3.
Example
- Example a block 0.20 m × 0.10 m × 0.050 m of mass 2.7 kg has V = 1.0 × 10−3 m3 and ρ = 2.7 × 103 kg/m3 (aluminium).
Mixtures
- Mixtures mixture density is total mass divided by total volume (200 mL water + 100 mL oil of 0.80 g/cm3 gives 280 g in 300 cm3, 0.93 g/cm3).
Temperature
- Temperature heating expands a liquid and lowers its density, driving convection.
Water
- Water densest near 4 °C, which is why ice floats and lakes freeze from the top.
Gases
- Gases density depends strongly on pressure and temperature.
Floating
- Floating a liquid with density below 1000 kg/m3 floats on water.
Section 2 of 7Pressure
P = F/A
- P = F/A perpendicular force per unit area, in pascals (1 Pa = 1 N/m2); a scalar.What the symbols mean: p = pressure (Pa = N m−2) · F = force acting at right angles to the surface (N) · A = area (m2)
Smaller area
- Smaller area the same force gives more pressure.
- (stiletto heel, drawing-pin point)
Net force
- Net force a pressure difference gives Fnet = ΔP × A.
Pascal's principle
- Pascal's principle a pressure change applied to an enclosed fluid is transmitted undiminished everywhere, the basis of hydraulic lifts, F1/A1 = F2/A2.
Pressure at depth
- P = P0 + ρgh;
- for immiscible layers add each term, the denser fluid at the bottom, and every interface is a surface of constant pressure.
U-tube
- U-tube equate pressures at the same level in the same liquid.
Mercury barometer
- Patm = ρHggh, so h = 1.01 × 105/(13 600 × 9.8) = 0.76 m.
Section 3 of 7Buoyancy
Buoyant force
- FB = ρfluidVdisplacedg, the weight of fluid displaced.
ρ
ρ is the density of the fluid, not of the object.
Vdisplaced
- Vdisplaced the whole volume if fully submerged, only the submerged part if floating.
Direction
- Direction upward, through the centre of the displaced fluid.
Apparent weight
- Apparent weight buoyancy does not change the object's weight but reduces its apparent weight in the fluid.
Section 4 of 7Continuity
1Volume flow rate
- Q = Av is the same everywhere for steady flow of an ideal fluid, so A1v1 = A2v2.
- (incompressible, non-viscous)
2Mass flow rate
- ρQ.
3Narrowing
- Narrowing halving the diameter quarters the area and quadruples the speed;
- a thumb over a hose end sends the spray farther.
4Narrow pipes
- Narrow pipes do not carry less fluid per second in steady flow.
5Junctions
- Junctions add flow rates, not speeds.
6Limit
- Limit continuity says nothing about pressure.
Section 5 of 7Bernoulli's equation
Bernoulli's equation
P + ½ρv2 + ρgy
- P + ½ρv2 + ρgy is constant along a streamline.
Narrow section
- Narrow section fluid is faster and the pressure lower.
Rising pipe at same speed
- Rising pipe at same speed pressure falls by ρgΔy.
Hole at depth h in a tank
- Hole at depth h in a tank exit speed v = √(2gh) (Torricelli).
Wing
- Wing lift comes from lower pressure over the faster-moving upper surface.
Section 6 of 7Key terms
| Term | Meaning |
|---|---|
| Density | Mass per unit volume. |
| Pressure | Perpendicular force per unit area. |
| Pascal's principle | Pressure change in an enclosed fluid transmits undiminished. |
| Buoyant force | Upward force equal to the weight of displaced fluid. |
| Continuity equation | A1v1 = A2v2 for incompressible flow. |
| Bernoulli's equation | P + ½ρv2 + ρgy constant along a streamline. |
| Volume flow rate | Volume passing a point per second, Q = Av. |
Section 7 of 7Exam technique
1
Using the object's density instead of the fluid's in the buoyant force.
2
Concluding a narrower pipe carries less fluid per second.
3
Using diameters instead of areas in continuity.
4
Assuming faster fluid means higher pressure — Bernoulli gives lower.
5
Adding speeds instead of flow rates at a junction.
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