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Bernoulli’s Equation

Original textbook reading.

Use continuity and Bernoulli for steady incompressible ideal flow in filled pipes. The new AP lessons add pressure, Pascal's principle and the model limits.

In this section we will learn about everything dealing with fluid flow through a pipe. More specifically, we will cover Bernoulli’s Equation and a little bit of the concept behind it.

Imagine a pipe with some volume. There is a certain amount of fluid with an area A1 and velocity v→1 and the same amount of fluid with a velocity v→2 and area A2. The color is used to coordinate with the image so don’t get confused. Ever notice that when you place a finger over the outlet of the hole on a hose, the water velocity increases?

The same can be applied to any pipe. Take for example in the figure. If the blue fluid were to enter from the left side for a certain time t with an area and velocity (assuming the flow is steady state and we are dealing with an incompressible fluid) then the same volume of orange fluid must emerge from the right side. The only difference is that the values are all inversely proportional to one another. Meaning that if A1>A2 then v→2>v→1 and vice versa.

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Figure 8.2.1 Equation of Continuity

Figure 8.2.1 Equation of Continuity
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Initial State

Fluid enters pipe with a small cross sectional area therefore having a larger velocity at the start.

Final State

The fluid flows through pipe and exits at a much larger cross sectional area therefore having a lower velocity.

This is the concept behind the equation of continuity. That the same volume of fluid entering from one side is emerging from the other side. The equation associated with this is:

A₁v₁ = A₂v₂ (Equation 8.2.1), where v₁ and v₂ are mean speeds normal to their respective cross-sections. This is the steady incompressible form of mass continuity.

Example Problem 8.2.1

A horizontal tapering pipe has inlet diameter 4 m and outlet diameter 2 m. A fluid particle travels 7 m through it with constant acceleration 3 m/s² along the flow. Assume steady incompressible flow with a smoothly varying area compatible with that acceleration. Find its inlet speed.

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Example Problem 8.2.1

Example Problem 8.2.1
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What’s Going on?

This is a flex coupling. It helps connect pipes of different diameters so that water can continue flowing no matter what configuration you have.

Step 1: Realize that this problem is a continuity equation

Even before tackling the problem, think about it conceptually. A fluid is traveling through a pipe with a velocity v→1. The pipe diameter changes from bigger to smaller, therefore the the cross sectional area goes from bigger to smaller as well. This change in area means that the velocity will increase. To keep the same volume flow rate through the pipe, the velocity will have to increase through the pipe with a smaller diameter.

Step 2: Use the continuity equation

A1v→1=A2v→2

where A1 is the area of a circle in this case since we have a pipe. We are given the diameter so in order to solve for the area, we need the

Step 4: Solve for the initial velocity

We now have an overall expression for the initial velocity ( v→1 ). Solving for v→2 from the continuity equation gives us:

v→2=(r1r2)2⋅v→1

Substituting v→2 from this equation into the kinematics equation and solving for v→1 will give:​
v→1=-2a→xL1-(r1r2)4

We have all the given values, so let’s solve our problem.

radius. Since Acircle=πr2 :

π(d12)2v→1=π(d22)2v→2

And simplifying it even further will give us:

π(r1)2v→1=π(r2)2v→2

Step 3: Use of kinematics

Since this fluid is accelerating over a given length in a given direction ( x -direction) with an initial and final velocity, we can use kinematics to help us solve our problem. Remember your kinematics Equation 3.2.1.​
Where v→x would be the final velocity v→2, v→0 is the initial velocity v→1 and x-x0 is the total length that the fluid travels across, which is L.

(v→2)2=(v→1)2+2⋅a→x⋅L​

 

Now that we have this under our belt, let’s move on to the main point of the chapter, which is Bernoulli’s Equation.

v₁ = √[2(3 m/s²)(7 m)/((4 m/2 m)⁴ − 1)] = √(42/15) m/s.

v₁ = 1.673 m/s.

As a check, the outlet must be faster because its cross-sectional area is smaller.

Since d₁/d₂ = 2, the area ratio is A₁/A₂ = 4. Continuity gives v₂ = 4v₁, not 2v₁.

v₂ = 6.693 m/s. Check: v₂² − v₁² = 42.0 m²/s² = 2aL.

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Figure 8.2.2 Bernoulli’s Equation

Fluid flows from the lower-left inlet to the upper-right outlet. H marks the elevation difference between the two sections, H₂ − H₁.
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Initial Conditions

The lower inlet has pressure P₁, speed v₁ and elevation H₁, measured from the chosen height datum.

Final Conditions

The upper outlet has pressure P₂, speed v₂ and elevation H₂. The pictured H marks the elevation difference H₂ − H₁, rather than a separately chosen absolute outlet height.

Bernoulli’s equation expresses conservation of mechanical energy per unit volume along a streamline for steady incompressible flow with negligible viscous losses. Pressure work, kinetic energy per unit volume, and gravitational potential energy per unit volume contribute to the sum below.

P1+12ρ(v→1)2+ρgH1=P2+12ρ(v→2)2+ρgH2

The term ½ρv² is kinetic energy per unit volume, with units J/m³ = Pa. Here v is the fluid speed.

The term ρgH is gravitational potential energy per unit volume relative to a chosen height datum. The elevation difference between a large tank’s surface and its outlet can drive efflux.

Imagine that a hole was created in the bottom of a wooden cylindrical vessel due to the wood rotting over time as shown below. At this point, the water starts to pour out of this hole. Knowing that there is a hole with distance H from the the top of the water level and that the vessel is open to the air, find the velocity exiting the hole .

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Example Problem 8.2.2

Example Problem 8.2.2
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Fluid Height

Imagine what would happen if the height of the water was higher? That would mean that more water would come out of the hole due to the added pressure that a higher water level adds.

Step 1: Set up your Bernoulli Equation

It should make sense that we are using Bernoulli’s equation because this is a fluid with varying heights, pressures and velocities. Let’s use Bernoulli’s Equation:

P1+12ρ(v→1)2+ρgH1=P2+12ρ(v→2)2+ρgH2​
Here the left side of the equation represents the top of the tank, while the right hand side represents the bottom of the tank where the hole is.

Step 2: Realize that the pressures are equal

How is that? Well in the problem statement, it was specified that the water was exposed to the open air, meaning that the pressure at the top is atmospheric pressure. The water coming out from the hole is also exposed to atmospheric pressure, therefore the pressures at both

points are the same. To make our lives easier let’s make the claim:

P1=P2=P​
Meaning that we can simplify the Bernoulli equation to just:

P+12ρ(v→1)2+ρgH1=P+12ρ(v→2)2+ρgH2

Step 3: Eliminate variables

We can clean this equation up even more to make it simpler. Since the pressures are equal, those will cancel out. Also since we set our datum to be at where the hole is, the height at that point is 0. So we can now write our equation as:

12ρ(v→1)2+ρgH1=12ρ(v→2)2+ρg(0)

continuity to help you estimate certain values and make educated guesses.

Solving for v→2 gives us:

v→2=A1A2v→1

The initial cross-sectional area of the vessel at

Which can be cleaned up to make it look like:

ρv→12+2ρgH1=ρv→22

And by canceling out the densities, we get:

v→12+2gH1=v→22

Step 4: Solve for the final velocity v→2

We can solve for v→2 to get:

v→2=v→12+2gH1

So this is our final equation.......SIKE. We can actually simplify this even further. How?

Step 5: Use concept of continuity to help simplify

What do we mean ? Use the equation of

the top of the tank is much larger than the hole that’s created at the bottom. Meaning that:

A1>A2

If the area at the top is much larger with respect to the area of the hole, the final velocity will be much larger than the initial velocity. So if A1>A2 holds to be true, then we can make another statement:

v→2>v→1

Neglect the free-surface speed only if the tank surface area is much larger than the opening area, A₁ ≫ A₂. Then v₁/v₂ = A₂/A₁ ≪ 1, and the outlet speed is approximately √(2gH₁).

v→2=2gH1.

Pause & recall

Pop Quiz 8.2.1 Continuity and Bernoulli’s Principle

Question 1 of 5 · 0 correct

AP Topic 8.4 · Read the worked solution

A fluid flows through the inlet of a pipe with diameter 1m and velocity 4m/s. The fluid exits at the outlet of the pipe which has a diameter of 1.5m. What is the velocity at this point?

Select one answer.
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Question 1

A fluid flows through the inlet of a pipe with diameter 1m and velocity 4m/s. The fluid exits at the outlet of the pipe which has a diameter of 1.5m. What is the velocity at this point?

  1. 4m/s

  2. 2.67m/s

  3. 1.78m/s

  4. 1m/s

Separate worked answer

Question 2

Given that the final velocity in a pipe system is 12m/s , what must be the ratio of A2:A1 in order to achieve an initial velocity of 3m/s?

  1. 1:4

  2. 3:1

  3. 2:2

  4. 4:1

  5. 1:1

Separate worked answer

Question 3

In steady incompressible lossless flow along a horizontal streamline, if fluid speed increases, its static pressure must:

  1. Increase

  2. Decrease

  3. Stay the Same

  4. None of the Above

Separate worked answer

Question 4

For steady incompressible flow through the pictured sections, rank the mean speeds from greatest to least (I–IV).

A fully filled horizontal pipe narrows in four labeled sections from A, widest, through B and C, to D, narrowest; steady flow moves from left to right. 1234

Match these labels to the numbered figure targets. Write your matches before opening the separate worked answer.

  • IV

  • III

  • II

  • I

Separate worked answer

Question 5

Assume the pictured pipe is horizontal and the flow is steady, incompressible, and lossless. Rank the static pressures from greatest to least (I–IV).

A fully filled horizontal pipe narrows in four labeled sections from A, widest, through B and C, to D, narrowest; steady flow moves from left to right. 1234

Match these labels to the numbered figure targets. Write your matches before opening the separate worked answer.

  • IV

  • III

  • II

  • I

Separate worked answer

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Reviewed physics notes (15)

These corrections keep the original lesson’s purpose while fixing errors in the source edition.

  • Products Av use normal speed, not an unconstrained vector velocity. — Reference 1
  • Clarifies that steady flow can have convective acceleration and that a constant-acceleration taper is an idealization. — Reference 1
  • Bernoulli is an energy balance, whereas continuity is mass conservation; they are not the same principle. — Reference 1
  • The term is energy density rather than the whole fluid’s kinetic energy. — Reference 1
  • Clarifies scalar energy density and height datum. — Reference 1
  • The numerical substitution mistakenly squares the diameter ratio instead of raising it to the fourth power. — Reference 1
  • Corrects the inlet speed; the original 2.8 m/s does not satisfy both continuity and constant-acceleration kinematics. — Reference 1
  • The source says the final area is larger even though diameter halves. — Reference 1
  • Area depends on the square of diameter. — Reference 1
  • Corrects outlet speed and verifies both governing equations. — Reference 1
  • A mere inequality A₁ > A₂ does not justify neglecting v₁; the area ratio must be small. — Reference 1
  • An area ratio is dimensionless; the source incorrectly attaches m² to ratio choices. — Reference 1
  • The marked decrease relies on Bernoulli’s assumptions. — Reference 1
  • Makes the continuity assumptions explicit for the image ranking. — Reference 1
  • Pressure cannot be ranked from area alone if elevation or head losses differ. — Reference 1

About this edition and its source ↗

Glossary and deeper reading · 7 refreshers

These editorial refreshers supplement the reading. Definitions and examples are added guidance; original source wording and recorded answers remain in their original context.

  • Fluid

    A fluid is a material that flows and continuously deforms under a sustained shear stress. Liquids and gases are both fluids, although their compressibility and other properties can differ greatly. For example, both water in a pipe and air flowing through a duct are fluids.

    Read more: Fluid in detail →

  • Velocity

    Velocity describes how position changes with time and includes direction. Instantaneous velocity describes one moment, while average velocity is displacement divided by elapsed time. For example, a car turning a corner can change velocity while maintaining the same speed.

    Read more: Variables of motion →

  • Incompressible fluid

    An incompressible-fluid model treats density as constant despite pressure changes in the modeled situation. This approximation often works for liquids over modest pressure ranges but is not a universal property of all fluids. For example, water flowing through a narrowing pipe can often be treated as incompressible.

    Read more: Incompressible fluid in detail →

  • Mechanical energy

    Mechanical energy is the sum of the kinetic and potential energies included in a model. It stays constant when transfers to or from other energy stores and across the chosen boundary are absent. For example, a pendulum’s mechanical energy can remain approximately constant while energy shifts between motion and gravitational configuration.

    Read more: Mechanical energy in detail →

  • Streamline

    A streamline is a curve tangent to the local fluid velocity at each point at one instant. In steady flow its shape stays fixed and fluid particles follow it, while in changing flow a streamline need not be a particle’s full path. For example, streamline arrows around a smooth obstacle show the local direction of the passing fluid.

    Read more: Streamline in detail →

  • Kinetic energy

    Kinetic energy is energy associated with motion relative to a chosen reference frame. For a nonrelativistic translating object it is one half of its mass times speed squared. For example, doubling a cart’s speed quadruples its translational kinetic energy when its mass stays fixed.

    Read more: Kinetic energy →

  • Gravitational potential energy

    Gravitational potential energy is energy associated with the relative positions of attracting masses. Near Earth, changes can be approximated by mass times gravitational field strength times height change when that field is nearly constant. For example, lifting a book increases the gravitational potential energy of the book–Earth system.

    Read more: Potential energy →

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