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๐ŸŽฏโญ INTERACTIVE LESSON

Bernoulli's Equation

Learn step-by-step with interactive practice!

Bernoulli's Equation - Complete Interactive Lesson

Part 1: Bernoulli's Equation Setup

๐Ÿ“œ Bernoulli's Equation โ€” Setup

Part 1 of 7 โ€” Fluids: Bernoulli's Equation

Bernoulli's Equation captures conservation of energy for a flowing fluid. It's the second pillar of AP fluids (alongside continuity), and it explains why airplanes fly, why your shower curtain pulls inward, and how a Venturi meter works.

In this lesson you will learn:

  • The full Bernoulli equation
  • The three energy-density terms (pressure, kinetic, gravitational)
  • The assumptions (incompressible, non-viscous, steady, along a streamline)
  • How to identify "two points" on a streamline for problem solving

Bernoulli's Equation

For an ideal fluid (incompressible, non-viscous, steady, irrotational) along a streamline:

P1+12ฯv12+ฯgy1=P2+12ฯv22+ฯgy2\boxed{P_1 + \tfrac{1}{2}\rho v_1^2 + \rho g y_1 = P_2 + \tfrac{1}{2}\rho v_2^2 + \rho g y_2}

Equivalently: P+12ฯv2+ฯgy=constantP + \tfrac{1}{2}\rho v^2 + \rho g y = \text{constant} along a streamline.

Each Term Has Units of Pressure (Pa)

TermMeaning
PPStatic pressure (Pa)
12ฯv2\tfrac{1}{2}\rho v^2Dynamic pressure / KE per volume (Pa)
ฯgy\rho g yGravitational PE per volume (Pa)

It's just energy conservation per unit volume of fluid.

Required Assumptions

  1. Incompressible โ€” ฯ\rho constant
  2. Non-viscous โ€” no internal friction
  3. Steady โ€” flow speed at each point doesn't change in time
  4. Along a streamline โ€” same fluid parcel from point 1 to point 2

Choosing Points 1 and 2 (the AP technique)

  • Pick where you know the most (PP, vv, yy all knowable).
  • Reservoir surface, pipe outlets, openings to atmosphere โ†’ known PP (PatmP_{atm}) and often vโ‰ˆ0v \approx 0.
  • Use one point where you have many unknowns? โ†’ No. Pick known points!

Bernoulli Concepts ๐ŸŽฏ

Bernoulli Setup Calculations ๐Ÿงฎ (g = 10, ฯw=1000\rho_w = 1000, Patm=1.0ร—105P_{atm} = 1.0\times10^{5} Pa)

Calculate each TERM of Bernoulli at the given point โ€” answer in pascals.

  1. Surface of an open tank (P=PatmP = P_{atm}, v=0v = 0, y=5.0y = 5.0 m). The ฯgy\rho g y term (Pa)?

  2. Same surface โ€” the 12ฯv2\tfrac{1}{2}\rho v^2 term (Pa)?

  3. A point inside a pipe with v=4.0v = 4.0 m/s. The dynamic pressure term 12ฯv2\tfrac{1}{2}\rho v^2 (Pa)?

Bernoulli Setup Reasoning ๐Ÿ”

Exit Quiz โ€” Bernoulli Setup โœ…

Part 2: Conservation of Energy in Fluids

โšก Conservation of Energy in Fluids

Part 2 of 7 โ€” Fluids: Bernoulli's Equation

Bernoulli's equation is just energy conservation, repackaged. Each term is an energy density. Understanding the link to mechanical energy makes Bernoulli intuitive โ€” it's 12mv2+mgy\tfrac{1}{2}mv^2 + mgy from kinematics, divided by volume, plus a pressure-work term.

In this lesson you will learn:

  • The derivation: work-energy theorem applied to a fluid parcel
  • Why pressure ร— volume is "flow work"
  • How each term maps to a familiar mechanics concept
  • A units check

Derivation Sketch

Consider a fluid parcel of volume VV moving from point 1 to point 2 along a streamline.

The work-energy theorem says:

Wnet=ฮ”KE+ฮ”PE(forย eachย unitย volume)W_{net} = \Delta KE + \Delta PE \quad \text{(for each unit volume)}

Forces doing work on the parcel:

  • Pressure forces from neighboring fluid: Wpressure=(P1โˆ’P2)VW_{pressure} = (P_1 - P_2) V
  • Gravity: appears in ฮ”PE\Delta PE

KE change per unit volume: 12ฯv22โˆ’12ฯv12\tfrac{1}{2}\rho v_2^2 - \tfrac{1}{2}\rho v_1^2. PE change per unit volume: ฯgy2โˆ’ฯgy1\rho g y_2 - \rho g y_1.

Combining:

(P1โˆ’P2)=(12ฯv22โˆ’12ฯv12)+(ฯgy2โˆ’ฯgy1)(P_1 - P_2) = (\tfrac{1}{2}\rho v_2^2 - \tfrac{1}{2}\rho v_1^2) + (\rho g y_2 - \rho g y_1)

Rearranging:

P1+12ฯv12+ฯgy1=P2+12ฯv22+ฯgy2P_1 + \tfrac{1}{2}\rho v_1^2 + \rho g y_1 = P_2 + \tfrac{1}{2}\rho v_2^2 + \rho g y_2

Mapping to Mechanics

MechanicsBernoulli (per unit volume)
KE = 12mv2\tfrac{1}{2}mv^212ฯv2\tfrac{1}{2}\rho v^2
PE = mgymgyฯgy\rho g y
Work by external forcePVP V โ†’ in Bernoulli, PP is energy density

Quick Sanity Check (Units)

  • [P]=Pa=N/m2=Nโ‹…m/m3=J/m3[P] = \text{Pa} = \text{N/m}^2 = \text{N}\cdot\text{m/m}^3 = \text{J/m}^3
  • [12ฯv2]=(kg/m3)(m/s)2=kgโ‹…mโˆ’1sโˆ’2=J/m3โœ“[\tfrac{1}{2}\rho v^2] = (\text{kg/m}^3)(\text{m/s})^2 = \text{kg}\cdot\text{m}^{-1}\text{s}^{-2} = \text{J/m}^3 โœ“
  • [ฯgy]=(kg/m3)(m/s2)(m)=J/m3โœ“[\rho g y] = (\text{kg/m}^3)(\text{m/s}^2)(\text{m}) = \text{J/m}^3 โœ“

Energy Conservation Concepts ๐ŸŽฏ

Energy-Density Calculations ๐Ÿงฎ (g = 10, ฯw=1000\rho_w = 1000)

  1. Compute kinetic energy per unit volume of water moving at 5 m/s (Pa).

  2. Compute gravitational PE per unit volume of water at y=8y = 8 m (Pa).

  3. The total P+12ฯv2+ฯgyP + \tfrac{1}{2}\rho v^2 + \rho g y at a point with P=90P = 90 kPa, v=2v = 2 m/s, y=4y = 4 m (Pa)?

Energy in Bernoulli Reasoning ๐Ÿ”

Exit Quiz โ€” Energy in Fluids โœ…

Part 3: Pressure-Speed Trade-off

๐Ÿ”„ The Pressureโ€“Speed Trade-off

Part 3 of 7 โ€” Fluids: Bernoulli's Equation

The most famous Bernoulli result: fast-moving fluid has lower pressure. This is what makes airfoils lift, atomizers spray, and shower curtains pull inward. AP loves to test this counter-intuitive idea.

In this lesson you will learn:

  • The Bernoulli effect at constant elevation
  • Why "lift" and "suction" happen
  • Real-world examples: airplane wings, chimneys, shower curtains
  • How to predict pressure direction from speed change

Horizontal Bernoulli

For a horizontal streamline (y1=y2y_1 = y_2):

P1+12ฯv12=P2+12ฯv22P_1 + \tfrac{1}{2}\rho v_1^2 = P_2 + \tfrac{1}{2}\rho v_2^2

So ฮ”P=12ฯ(v12โˆ’v22)\Delta P = \tfrac{1}{2}\rho (v_1^2 - v_2^2).

Where the fluid is faster, the pressure is lower.

Real-World Examples

PhenomenonWhy
Airplane wing (lift)Faster air over curved top โ†’ lower pressure on top โ†’ net upward force
Atomizer/perfume sprayFast air over a tube tip โ†’ low PP at top โ†’ liquid pushed up by atmospheric pressure
Shower curtain pulled inFalling water drags air faster on inside โ†’ lower PP โ†’ curtain pushed in
Wind blowing roof offFast wind over roof โ†’ low PP above โ†’ high PP below pushes roof up

A Common Misconception

โŒ "Lower pressure pulls things into the fast stream." โœ… Higher pressure on the OTHER side PUSHES things toward the fast stream. Pressure only pushes.

Linking to Continuity

A1v1=A2v2A_1 v_1 = A_2 v_2 tells you HOW the speed changes (geometry). Bernoulli tells you HOW the pressure responds (energy). Both are needed for venturi-style problems. (Coming in Part 6.)

Pressure-Speed Trade-off ๐ŸŽฏ

Pressure-Speed Calculations ๐Ÿงฎ (ฯw=1000\rho_w = 1000, ฯair=1.2\rho_{air} = 1.2)

  1. A horizontal pipe carries water at 2 m/s where P=150P = 150 kPa. At a constriction it speeds up to 8 m/s. Pressure at the constriction (kPa)?

  2. Air flows over a wing at 50 m/s on top and 40 m/s on bottom. Pressure difference (Pa, top vs bottom: ฮ”P=Pbottomโˆ’Ptop\Delta P = P_{bottom} - P_{top})?

  3. A horizontal water pipe widens. At point 1: v1=6v_1 = 6 m/s, P1=100P_1 = 100 kPa. At point 2: v2=2v_2 = 2 m/s. P2P_2 in kPa?

Pressure-Speed Reasoning ๐Ÿ”

Exit Quiz โ€” Pressure-Speed Trade-off โœ…

Part 4: Torricelli's Theorem

๐Ÿšฟ Torricelli's Theorem

Part 4 of 7 โ€” Fluids: Bernoulli's Equation

Torricelli's Theorem is the classic Bernoulli application: water draining out of a hole in a tank flows like a free-falling object. It's a guaranteed AP Physics 1 favorite โ€” fast and elegant.

In this lesson you will learn:

  • How to derive v=2ghv = \sqrt{2gh} from Bernoulli
  • The "large reservoir" approximation
  • Time-of-flight for a horizontal jet exiting a tank
  • Range of the projected stream

Torricelli's Theorem

Setup: An open tank with a small hole of negligible cross-section, depth hh below the free surface. Both the surface (point 1) and the hole (point 2) are open to atmosphere โ‡’ P1=P2=PatmP_1 = P_2 = P_{atm}.

Bernoulli:

Patm+12ฯv12+ฯgh=Patm+12ฯv22+0P_{atm} + \tfrac{1}{2}\rho v_1^2 + \rho g h = P_{atm} + \tfrac{1}{2}\rho v_2^2 + 0

Atmospheric terms cancel. Since the tank is large, v1โ‰ˆ0v_1 \approx 0. So:

ฯgh=12ฯv22โ€…โ€Šโ‡’โ€…โ€Šv2=2gh\rho g h = \tfrac{1}{2}\rho v_2^2 \;\Rightarrow\; \boxed{v_2 = \sqrt{2 g h}}

This is the same as a freely-falling object dropped from height hh! That's the "Torricelli" insight.

Conditions for Validity

  • Hole area โ‰ช\ll tank area (so v1โ‰ˆ0v_1 \approx 0).
  • Both surfaces exposed to same external pressure.
  • Ideal fluid (no viscous losses).

Projectile Range of the Jet

If the hole is at height HH above the ground, the jet exits horizontally at speed v=2ghv = \sqrt{2gh} and falls under gravity:

  • Time to ground: t=2H/gt = \sqrt{2H/g}
  • Horizontal range: R=vโ€‰t=2ghโ‹…2H/g=2hHR = v \, t = \sqrt{2gh} \cdot \sqrt{2H/g} = 2\sqrt{hH}

Memorable result: R=2hHR = 2\sqrt{hH}. Maximum range when h=Hh = H (hole at half-height).

Torricelli Concepts ๐ŸŽฏ

Torricelli Calculations ๐Ÿงฎ (g = 10)

  1. Water in a large tank has surface 5.0 m above a small hole. Exit speed (m/s)?

  2. Same tank โ€” hole is 1.25 m above the ground. Time for the jet to hit the ground (s, 2 sig fig)?

  3. Same tank โ€” horizontal range of the jet (m)?

Torricelli Reasoning ๐Ÿ”

Exit Quiz โ€” Torricelli's Theorem โœ…

Part 5: Real-World Applications

๐ŸŒ Real-World Applications

Part 5 of 7 โ€” Fluids: Bernoulli's Equation

Bernoulli isn't just an exam formula โ€” it explains lift, plumbing, weather, sports, and your shower curtain. AP often presents qualitative scenarios where you must identify the Bernoulli effect at work.

In this lesson you will explore:

  • Airfoil lift (qualitative + estimate)
  • Venturi meters and flow measurement
  • Pitot tubes (airplane airspeed)
  • Atomizers and chimneys

Application Catalog

1. Airfoil / Lift

  • A wing's shape and its tilt (angle of attack) turn the oncoming air downward. In doing so, the air flowing over the top speeds up and the air underneath slows slightly.
  • The speeds are measured or given; Bernoulli then says faster air on top โ‡’ lower PP on top.
  • Pressure difference ร— wing area = lift force.
  • A common textbook story says air over the top must travel a longer path and "meet up" with the air underneath at the trailing edge. That is false: nothing forces the two streams to rejoin, and air over the top actually reaches the trailing edge first. Bernoulli explains lift from the speed difference, not from equal travel times.

Fliftโ‰ˆฮ”Pโ‹…A=12ฯair(vtop2โˆ’vbot2)โ€‰AF_{lift} \approx \Delta P \cdot A = \tfrac{1}{2}\rho_{air}(v_{top}^2 - v_{bot}^2)\, A

2. Venturi Meter (flow measurement)

  • A pipe with a narrow throat and a U-tube manometer between wide and narrow.
  • Difference in heights of the manometer fluid โ†’ ฮ”P\Delta P โ†’ using continuity + Bernoulli, solve for vv and hence QQ.

3. Pitot Tube (airspeed)

  • Has a forward-facing port (stagnation point, v=0v = 0, P=PstagP = P_{stag}) and a side port (flow speed vv, P=PstaticP = P_{static}).
  • Bernoulli at constant height: Pstag=Pstatic+12ฯv2P_{stag} = P_{static} + \tfrac{1}{2}\rho v^2.
  • v=2(Pstagโˆ’Pstatic)/ฯv = \sqrt{2(P_{stag} - P_{static})/\rho}.

4. Atomizer / Spray Bottle

  • Squeezing air across a vertical tube creates fast horizontal flow โ†’ low PP at top.
  • Atmospheric pressure pushes liquid up the tube and into the air stream.

5. Chimney Effect

  • Wind across a chimney top โ†’ low PP at top โ†’ draws smoke up.

Application Concepts ๐ŸŽฏ

Application Calculations ๐Ÿงฎ (ฯair=1.2\rho_{air} = 1.2, ฯw=1000\rho_w = 1000, g = 10)

  1. A Pitot tube on an airplane reads Pstagโˆ’Pstatic=600P_{stag} - P_{static} = 600 Pa. Airspeed (m/s)?

  2. An airfoil has vtop=80v_{top} = 80 m/s, vbot=60v_{bot} = 60 m/s. Pressure difference ฮ”P=Pbotโˆ’Ptop\Delta P = P_{bot} - P_{top} (Pa)?

  3. Wing area = 12 m2m^{2}. Lift force using the ฮ”P\Delta P from Q2 (N)?

Application Reasoning ๐Ÿ”

Exit Quiz โ€” Real-World Applications โœ…

Part 6: Combined Continuity + Bernoulli

๐Ÿ› ๏ธ Combined Continuity + Bernoulli

Part 6 of 7 โ€” Fluids: Bernoulli's Equation

The hardest AP fluids problems combine BOTH governing equations: continuity to find unknown speeds from geometry, then Bernoulli to find unknown pressures (or vice versa). This part is the workshop where you put them together.

Key combination workflow:

  1. Identify two points on the same streamline.
  2. Continuity: A1v1=A2v2A_1 v_1 = A_2 v_2 โ†’ solve for the unknown speed.
  3. Bernoulli: P1+12ฯv12+ฯgy1=P2+12ฯv22+ฯgy2P_1 + \tfrac{1}{2}\rho v_1^2 + \rho g y_1 = P_2 + \tfrac{1}{2}\rho v_2^2 + \rho g y_2 โ†’ solve for the unknown pressure.

Strategy Cheat Sheet

GivenUse
Areas + one vvContinuity for unknown vv
Speeds + one PPBernoulli for unknown PP
Manometer readingฮ”P=ฯmangh\Delta P = \rho_{man} g h then Bernoulli
Tank with holeTorricelli (special-case Bernoulli)
Pitot tubePstag=Pstatic+12ฯv2P_{stag} = P_{static} + \tfrac{1}{2}\rho v^2

Worked Venturi

A horizontal Venturi: wide section A1=0.10A_1 = 0.10 m2m^{2} has v1=2v_1 = 2 m/s, P1=200P_1 = 200 kPa; narrow throat A2=0.025A_2 = 0.025 m2m^{2}. Find P2P_2.

Step 1 โ€” Continuity: v2=v1(A1/A2)=2ร—4=8v_2 = v_1 (A_1/A_2) = 2 \times 4 = 8 m/s.

Step 2 โ€” Bernoulli (horizontal): P2=P1+12ฯ(v12โˆ’v22)=200,000+12(1000)(4โˆ’64)=170,000ย PaP_2 = P_1 + \tfrac{1}{2}\rho(v_1^2 - v_2^2) = 200{,}000 + \tfrac{1}{2}(1000)(4 - 64) = 170{,}000 \text{ Pa}

So P2=170P_2 = 170 kPa. The throat pressure dropped by 30 kPa.

Combined Pipe with Elevation Change

A pipe carries water from A1=0.04A_1 = 0.04 m2m^{2}, v1=1v_1 = 1 m/s, y1=0y_1 = 0, P1=300P_1 = 300 kPa upward to A2=0.01A_2 = 0.01 m2m^{2}, y2=5y_2 = 5 m. Find P2P_2.

  • v2=4v_2 = 4 m/s by continuity.
  • Bernoulli: P2=300,000+12(1000)(1โˆ’16)+1000(10)(0โˆ’5)=300,000โˆ’7500โˆ’50,000=242,500P_2 = 300{,}000 + \tfrac{1}{2}(1000)(1 - 16) + 1000(10)(0 - 5) = 300{,}000 - 7500 - 50{,}000 = 242{,}500 Pa.

Combined Application Quick MC ๐ŸŽฏ

Combined Workshop ๐Ÿงฎ (ฯw=1000\rho_w = 1000, g = 10)

  1. Horizontal Venturi: A1=0.020A_1 = 0.020 m2m^{2}, v1=3v_1 = 3 m/s, P1=250P_1 = 250 kPa; A2=0.010A_2 = 0.010 m2m^{2}. Find P2P_2 (kPa).

  2. A vertical pipe: A1=0.005A_1 = 0.005 m2m^{2}, v1=4v_1 = 4 m/s, y1=0y_1 = 0, P1=400P_1 = 400 kPa. Upper end: A2=0.005A_2 = 0.005 m2m^{2} (same area), y2=10y_2 = 10 m. Find P2P_2 (kPa).

  3. Same pipe, but upper end narrows to A2=0.0025A_2 = 0.0025 m2m^{2}. Find P2P_2 (kPa).

Combined-Reasoning Drill ๐Ÿ”

Exit Quiz โ€” Combined Workshop โœ…

Part 7: Synthesis & AP Review

๐ŸŽฏ Synthesis & AP Review โ€” Bernoulli

Part 7 of 7 โ€” Fluids: Bernoulli's Equation

You've completed the full AP Physics 1 fluids progression: density, pressure, buoyancy, continuity, and Bernoulli. This synthesis ties Bernoulli together with continuity into the integrated mental model AP expects โ€” fast questions, big-picture reasoning, and confident calculations.

Big Ideas Recap:

  • P1+12ฯv12+ฯgy1=P2+12ฯv22+ฯgy2P_1 + \tfrac{1}{2}\rho v_1^2 + \rho g y_1 = P_2 + \tfrac{1}{2}\rho v_2^2 + \rho g y_2
  • Faster fluid = lower pressure (at same height)
  • Torricelli: v=2ghv = \sqrt{2gh}
  • Pitot: Pstagโˆ’Pstatic=12ฯv2P_{stag} - P_{static} = \tfrac{1}{2}\rho v^2
  • Combined Continuity + Bernoulli unlocks Venturi-type problems

Bernoulli AP Cheat Sheet

ConceptEquation
Bernoulli (general)P+12ฯv2+ฯgy=P + \tfrac{1}{2}\rho v^2 + \rho g y = const
Horizontal pipeP1+12ฯv12=P2+12ฯv22P_1 + \tfrac{1}{2}\rho v_1^2 = P_2 + \tfrac{1}{2}\rho v_2^2
Constant area pipeP1+ฯgy1=P2+ฯgy2P_1 + \rho g y_1 = P_2 + \rho g y_2 (just hydrostatic)
Torricelliv=2ghv = \sqrt{2gh}
Pitot tubev=2(Pstagโˆ’Pstatic)/ฯv = \sqrt{2(P_{stag} - P_{static})/\rho}
Lift (rough)Fliftโ‰ˆ12ฯair(vt2โˆ’vb2)AF_{lift} \approx \tfrac{1}{2}\rho_{air}(v_t^2 - v_b^2) A
Continuity (incompressible)A1v1=A2v2A_1 v_1 = A_2 v_2

AP Reasoning Patterns

  1. "Pressure drops where fluid speeds up" โ€” Bernoulli at same height.
  2. "Tank drains faster when..." โ€” Torricelli, larger hh โ‡’ larger vv.
  3. "Wing lift comes from..." โ€” pressure difference from speed difference.
  4. "Two parallel boats drift together" โ€” Bernoulli โ‡’ low PP between them.
  5. "Combined speed + pressure problem" โ€” apply continuity, then Bernoulli.

Common Pitfalls

  • โŒ Forgetting that ALL Bernoulli terms are per unit volume (Pa).
  • โŒ Confusing ฯfluid\rho_{fluid} with ฯair\rho_{air} in lift problems.
  • โŒ Applying Bernoulli to viscous or turbulent flow (e.g., long thin pipes with friction).
  • โŒ Forgetting to use continuity FIRST when speeds aren't given directly.

Final Mental Model

Bernoulli = "energy conservation per unit volume along a streamline." Find your two points, identify PP, vv, yy at each, and let energy do the rest.

AP Synthesis MC ๐ŸŽฏ

AP Synthesis Calculations ๐Ÿงฎ (ฯw=1000\rho_w = 1000, ฯair=1.2\rho_{air} = 1.2, g = 10)

  1. A large open tank's water surface is 10 m above a small hole. Exit speed (m/s)?

  2. Horizontal pipe: A1=0.04A_1 = 0.04 m2m^{2}, v1=1v_1 = 1 m/s, P1=200P_1 = 200 kPa; A2=0.01A_2 = 0.01 m2m^{2}. Find P2P_2 (kPa).

  3. A Pitot tube on a small drone reads ฮ”P=24\Delta P = 24 Pa (ฯair=1.2\rho_{air} = 1.2). Airspeed (m/s)?

AP Concept Synthesis ๐Ÿ”

Exit Quiz โ€” Bernoulli Synthesis โœ