Without hydrostatic pressure

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In the case where flow occurs in a gas or in a situation where height variations are minimal, the effect of hydrostatic pressure can be neglected.

Without hydrostatic pressure, Bernoulli's law reduces to the sum of a term associated with kinetic energy, and thus with velocity squared, and the pressure existing at each location remaining constant. This implies that if velocity increases, pressure decreases, and vice versa.

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Mechanisms

Concept

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Code
Concept
Bernoulli's law, without hydrostatic pressure
Overpass and crossing of vehicles on the road
Pitot tube

Mechanisms

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Bernoulli's law, without hydrostatic pressure

Concept

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If energy is conserved and the medium flows without deforming, it follows that the density between two points must be equal, which is the premise leading to Bernoulli's law.

Considering the energy density calculated at points 1 and 2:
• The scientific energy density depends on the liquid density ($\rho_w$), at point 1 The mean Speed of Fluid in Point 1 ($v_1$), and at point 2 The mean Speed of Fluid in Point 2 ($v_2$).
• The potential energy density in general corresponds to the pressure in column 1 ($p_1$) at point 1 and the pressure in column 2 ($p_2$).
we have the relation

$\displaystyle\frac{1}{2} \rho v_1 ^2 + p_1 =\displaystyle\frac{1}{2} \rho v_2 ^2 + p_2 $



This expression can be rewritten with the variación de la Presión ($\Delta p$)

$ \Delta p = p_2 - p_1 $



with the average speed ($\bar{v}$)

$ \bar{v} = \displaystyle\frac{ v_1 + v_2 }{2}$



and with the speed difference between surfaces ($\Delta v$)

$ \Delta v = v_2 - v_1 $



finally resulting in

$ \Delta p = - \rho \bar{v} \Delta v $

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Pitot tube

Description

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The speed of an aircraft is determined using a device called a Pitot tube. It consists of two openings: one at the front (known as the \\"leading edge\\") and the other on the side. At the leading edge, the velocity is zero, while at the side opening, it represents the speed at which the aircraft is moving relative to the surrounding air. Inside the openings, there are two tubes filled with fluid, allowing the measurement of the pressure difference between the two points. By applying Bernoulli's equation, it is possible to calculate the velocity of the aircraft using the pressure difference and the fluid density.



Particularly, the velocity at the tip of the Pitot tube is zero, meaning that the speed difference between surfaces ($\Delta v$) reduces to the velocity at the side orifice ($\Delta v = v$), while the average speed ($\bar{v}$) equals half the velocity ($\bar{v}=v/2$). Since the velocity corresponds to the aircraft's speed, it can be determined by measuring pressure using the equation:

$v=\sqrt{\displaystyle\frac{2 \Delta p}{\rho}}$

It's worth noting that this equation requires density, which varies with the altitude at which the aircraft is flying.

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Overpass and crossing of vehicles on the road

Description

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When overtaking a car on the road, a situation arises where a higher-speed airflow is generated between the two vehicles, resulting in lower pressure in that area. Consequently, the pressure on the outer sides of the cars causes them to attract each other.

As vehicles cross paths, the relative velocity between them decreases and approaches rest, generating higher pressure between them and causing them to move away from each other.



The same phenomenon occurs when two boats cross paths. If the crossing takes place in a narrow channel, both helmsmen must steer their vessels towards the opposite side to prevent the repulsive force from causing a collision with the channel's edge.

To explain why this happens, we can apply the equation the variación de la Presión ($\Delta p$) with the average speed ($\bar{v}$) and the speed difference between surfaces ($\Delta v$) with the density ($\rho$) using

$ \Delta p = - \rho \bar{v} \Delta v $

Therefore, it can be seen that if there is a velocity gradient, it is inversely proportional to the pressure gradient. If one increases, the other decreases, explaining why overtaking cars exhibit higher velocity between them, leading to a reduction in pressure between them, causing mutual suction. Conversely, if they cross, the velocity between them is approximately zero, generating a pressure gradient that pushes them apart.

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Model

Concept

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Variables

Symbol
Text
Variables
Units
$\bar{v}$
v_m
Average speed
m/s
$e$
e
Energy density
J/m^3
$e_1$
e_1
Energy density in 1
J/m^3
$e_2$
e_2
Energy density in 2
J/m^3
$v$
v
Mean Speed of Fluid
m/s
$v_1$
v_1
Mean Speed of Fluid in Point 1
m/s
$v_2$
v_2
Mean Speed of Fluid in Point 2
m/s
$p_1$
p_1
Pressure in column 1
Pa
$p_2$
p_2
Pressure in column 2
Pa
$\Delta v$
Dv
Speed difference between surfaces
m/s
$p_t$
p_t
Water column pressure
Pa

Parameters

Symbol
Text
Variables
Units


Selected parameter

Symbol
Variables
Value
Units
MKS Value
MKS Units

Calculations

Symbol
Equation
Solved
Translated

Equation

#
Equation

$ \Delta p = - \rho \bar{v} \Delta v $

Dp = - rho * v_m * Dv


$ \Delta p = p_2 - p_1 $

Dp = p_2 - p_1


$ \Delta v = v_2 - v_1 $

Dv = v_2 - v_1


$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $

e = rho * v ^ 2 / 2 + p


$ e_1 =\displaystyle\frac{1}{2} \rho v_1 ^2+ p $

e = rho * v ^ 2 / 2 + p


$ e_2 =\displaystyle\frac{1}{2} \rho v_2 ^2+ p $

e = rho * v ^ 2 / 2 + p


$ e_1 = e_2 $

e_1 = e_2


$\displaystyle\frac{1}{2} \rho v_1 ^2 + p_1 =\displaystyle\frac{1}{2} \rho v_2 ^2 + p_2 $

rho * v_1 ^2/2 + p_1 = rho * v_2 ^2/2 + p_2


$ \bar{v} = \displaystyle\frac{ v_1 + v_2 }{2}$

v_m = ( v_1 + v_2 )/2

ID:(15498, 0)



Energy density, without hydrostatic pressure

Equation

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Since a fluid or gas is a continuum, the concept of energy can no longer be associated with a specific mass. However, it is possible to consider the energy contained in a volume of the continuum, and by dividing it by the volume itself, we obtain the energy density ($e$). Therefore, with the density ($\rho$), the mean Speed of Fluid ($v$) and the water column pressure ($p_t$), we have:

$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $

$\rho$
Density
$kg/m^3$
$e$
Energy density
$J/m^3$
$v$
Mean Speed of Fluid
$m/s$
$p$
Water column pressure
$Pa$

Another useful equation is the one corresponding to the conservation of energy, which is applicable in cases where viscosity, a process that leads to energy loss, can be neglected. If we consider the classic energy equation $E$, which takes into account kinetic energy, gravitational potential energy, and an external force displacing the liquid over a distance $\Delta z$, it can be expressed as:

$E=\displaystyle\frac{m}{2}v^2+mgh+F\Delta x$



If we consider the energy within a volume $\Delta x\Delta y\Delta z$, we can replace the mass with:

$m=\rho \Delta x\Delta y\Delta z$



And since pressure is given by:

$F=p \Delta S =p \Delta y\Delta z$



We obtain the equation for energy density:

$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $



which corresponds to the Bernoulli equation.

In the absence of viscosity, the conservation of energy implies that the energy density ($e$) is constant at any point in the fluid. Therefore, knowing the velocity and/or pressure at any location in the fluid is sufficient to establish a relationship between velocity and pressure at any point in the fluid.

ID:(15496, 0)



Conservation of energy density

Equation

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If energy is conserved within the flowing volumes, then the energy density in 1 ($e_1$) and the energy density in 2 ($e_2$) must be equal:

$ e_1 = e_2 $

$e_1$
Energy density in 1
$J/m^3$
$e_2$
Energy density in 2
$J/m^3$

This is only possible if viscosity is negligible, as it is associated with energy diffusion, and there are no vortices present, which themselves exhibit energy differences due to varying tangential velocities along the vortex radius.

ID:(15499, 0)



Energy density, without hydrostatic pressure (1)

Equation

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Since a fluid or gas is a continuum, the concept of energy can no longer be associated with a specific mass. However, it is possible to consider the energy contained in a volume of the continuum, and by dividing it by the volume itself, we obtain the energy density ($e$). Therefore, with the density ($\rho$), the mean Speed of Fluid ($v$) and the water column pressure ($p_t$), we have:

$ e_1 =\displaystyle\frac{1}{2} \rho v_1 ^2+ p_1 $

$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $

$\rho$
Density
$kg/m^3$
$e$
$e_1$
Energy density in 1
$J/m^3$
$v$
$v_1$
Mean Speed of Fluid in Point 1
$m/s$
$p$
$p_1$
Pressure in column 1
$Pa$

Another useful equation is the one corresponding to the conservation of energy, which is applicable in cases where viscosity, a process that leads to energy loss, can be neglected. If we consider the classic energy equation $E$, which takes into account kinetic energy, gravitational potential energy, and an external force displacing the liquid over a distance $\Delta z$, it can be expressed as:

$E=\displaystyle\frac{m}{2}v^2+mgh+F\Delta x$



If we consider the energy within a volume $\Delta x\Delta y\Delta z$, we can replace the mass with:

$m=\rho \Delta x\Delta y\Delta z$



And since pressure is given by:

$F=p \Delta S =p \Delta y\Delta z$



We obtain the equation for energy density:

$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $



which corresponds to the Bernoulli equation.

In the absence of viscosity, the conservation of energy implies that the energy density ($e$) is constant at any point in the fluid. Therefore, knowing the velocity and/or pressure at any location in the fluid is sufficient to establish a relationship between velocity and pressure at any point in the fluid.

ID:(15496, 1)



Energy density, without hydrostatic pressure (2)

Equation

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Since a fluid or gas is a continuum, the concept of energy can no longer be associated with a specific mass. However, it is possible to consider the energy contained in a volume of the continuum, and by dividing it by the volume itself, we obtain the energy density ($e$). Therefore, with the density ($\rho$), the mean Speed of Fluid ($v$) and the water column pressure ($p_t$), we have:

$ e_2 =\displaystyle\frac{1}{2} \rho v_2 ^2+ p_2 $

$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $

$\rho$
Density
$kg/m^3$
$e$
$e_2$
Energy density in 2
$J/m^3$
$v$
$v_2$
Mean Speed of Fluid in Point 2
$m/s$
$p$
$p_2$
Pressure in column 2
$Pa$

Another useful equation is the one corresponding to the conservation of energy, which is applicable in cases where viscosity, a process that leads to energy loss, can be neglected. If we consider the classic energy equation $E$, which takes into account kinetic energy, gravitational potential energy, and an external force displacing the liquid over a distance $\Delta z$, it can be expressed as:

$E=\displaystyle\frac{m}{2}v^2+mgh+F\Delta x$



If we consider the energy within a volume $\Delta x\Delta y\Delta z$, we can replace the mass with:

$m=\rho \Delta x\Delta y\Delta z$



And since pressure is given by:

$F=p \Delta S =p \Delta y\Delta z$



We obtain the equation for energy density:

$ e =\displaystyle\frac{1}{2} \rho v ^2+ p $



which corresponds to the Bernoulli equation.

In the absence of viscosity, the conservation of energy implies that the energy density ($e$) is constant at any point in the fluid. Therefore, knowing the velocity and/or pressure at any location in the fluid is sufficient to establish a relationship between velocity and pressure at any point in the fluid.

ID:(15496, 2)



Bernoulli equation, without hydrostatic pressure

Equation

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In the case of Bernoulli's law [1], in the case where there is no hydrostatic pressure, we have the density ($\rho$), the pressure in column 1 ($p_1$), the pressure in column 2 ($p_2$), the mean Speed of Fluid in Point 1 ($v_1$) and the mean Speed of Fluid in Point 2 ($v_2$):

$\displaystyle\frac{1}{2} \rho v_1 ^2 + p_1 =\displaystyle\frac{1}{2} \rho v_2 ^2 + p_2 $

$\rho$
Density
$kg/m^3$
$v_1$
Mean Speed of Fluid in Point 1
$m/s$
$v_2$
Mean Speed of Fluid in Point 2
$m/s$
$p_1$
Pressure in column 1
$Pa$
$p_2$
Pressure in column 2
$Pa$



The Bernoulli equation assumes the conservation of energy density, implying the absence of viscosity and turbulence, making its application in this case limited.

The Bernoulli equation can serve as a foundation for modeling the process, but it must necessarily be supplemented with a model that accounts for the possibility of including the effects of turbulence.

[1] "Hydrodynamica" (Hidrodinamica), Daniel Bernoulli, Typis Joh. Henr. Deckeri (1738)

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Pressure difference

Equation

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When two liquid columns are connected with the pressure in column 1 ($p_1$) and the pressure in column 2 ($p_2$), a the pressure difference ($\Delta p$) is formed, which is calculated according to the following formula:

$ \Delta p = p_2 - p_1 $

$p_1$
Pressure in column 1
$Pa$
$p_2$
Pressure in column 2
$Pa$
$\Delta p$
Variación de la Presión
$Pa$



the pressure difference ($\Delta p$) represents the pressure difference that will cause the liquid to flow from the taller column to the shorter one.

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Average speed

Equation

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The average speed ($\bar{v}$) is with the mean Speed of Fluid in Point 1 ($v_1$) and the mean Speed of Fluid in Point 2 ($v_2$) is

$ \bar{v} = \displaystyle\frac{ v_1 + v_2 }{2}$

$\bar{v}$
Average speed
$m/s$
$v_1$
Mean Speed of Fluid in Point 1
$m/s$
$v_2$
Mean Speed of Fluid in Point 2
$m/s$

ID:(15501, 0)



Speed difference

Equation

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The speed difference between surfaces ($\Delta v$) is with the mean Speed of Fluid in Point 1 ($v_1$) and the mean Speed of Fluid in Point 2 ($v_2$) is

$ \Delta v = v_2 - v_1 $

$v_1$
Mean Speed of Fluid in Point 1
$m/s$
$v_2$
Mean Speed of Fluid in Point 2
$m/s$
$\Delta v$
Speed difference between surfaces
$m/s$

ID:(15502, 0)



Bernoulli equation, variations

Equation

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The variación de la Presión ($\Delta p$) can be calculated from the average speed ($\bar{v}$) and the speed difference between surfaces ($\Delta v$) with the density ($\rho$) using

$ \Delta p = - \rho \bar{v} \Delta v $

$\bar{v}$
Average speed
$m/s$
$\rho$
Density
$kg/m^3$
$\Delta v$
Speed difference between surfaces
$m/s$
$\Delta p$
Variación de la Presión
$Pa$

In the case where there is no hystrostatic pressure, Bernoulli's law for the liquid density ($\rho_w$), the pressure in column 1 ($p_1$), the pressure in column 2 ($p_2$), the mean Speed of Fluid in Point 1 ($v_1$) and the mean Speed of Fluid in Point 2 ($v_2$)

$\displaystyle\frac{1}{2} \rho v_1 ^2 + p_1 =\displaystyle\frac{1}{2} \rho v_2 ^2 + p_2 $



can be rewritten with the variación de la Presión ($\Delta p$)

$ \Delta p = p_2 - p_1 $



and keeping in mind that

$v_2^2 - v_1^2 = \displaystyle\frac{1}{2}(v_2-v_1)(v_1+v_2)$



with

$ \bar{v} = \displaystyle\frac{ v_1 + v_2 }{2}$



and

$ \Delta v = v_2 - v_1 $



you have to

$ \Delta p = - \rho \bar{v} \Delta v $

which allows us to see the effect of the average speed of a body and the difference between its surfaces, as observed in an airplane or bird wing.

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