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Hydraulics, open channels and fluid power

Fluid force on a right-angle elbow (x-component)

Horizontal component of the force of the fluid on an elbow that turns the flow from the +x direction to +y, from the inlet gauge pressure, area and speed.

Ref
HYD-34
Rev
v1
Field
Hydraulics, open channels and fluid power
Result
Fx [N]

A steady flow entering an elbow along +x and leaving along +y changes its momentum, so the fluid pushes on the elbow. Using gauge pressures, the x-component of the force of the fluid on the elbow is Fx = p₁A₁ + ρ Q U₁, and the y-component is Fy = −p₂A₂ − ρ Q U₂. The weight of the fluid and the elbow are excluded, so thrust blocks must also carry them. Here Q = A U at each section.

Horizontal component of the force of the fluid on an elbow that turns the flow from the +x direction to +y, from the inlet gauge pressure, area and speed. The vertical component, Fy = −p₂A₂ − ρQU₂, and the resultant are in the derived rows.

Calculator

Solve for
N
Pa
1,0001e8
Pa
1,0001e8
m²
1e-41
m²
1e-41
kg/m³
5002,000
m³/s
1e-410
m/s
0.0150
m/s
0.0150
  • Force y-component, −p₂A₂ − ρ Q U₂−1,540 N
  • Resultant force magnitude2,556 N
  • Direction of the resultant, from +x−37.05 °

What drives the result

Each variable is moved across its typical range while the others stay at the values above. The longest bar is the key driver.

Force on the elbow, x-component (N) current value 2,040 N
p1Inlet gauge pressureKey driver
501,000,000
A1Inlet area
60200,000
QDischarge
2,00022,000
U1Inlet mean speed
2,0003,000
ρLiquid density
2,0202,080
p2Outlet gauge pressure
A2Outlet area
U2Outlet mean speed
  • The fluid pushes the elbow with 2,040 N in x and −1,540 N in y, a resultant of 2,556 N.
  • Most of the force is the pressure; the momentum part is only 40 N in x, which is why thrust blocks depend mainly on line pressure.
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing (N)Local stepChange in result
p1 Inlet gauge pressure1,000 to 1e8 Pa501,000,0001,000,000+10%+9.8 %
A1 Inlet area1e-4 to 1 m²60200,000200,000+10%+9.8 %
Q Discharge1e-4 to 10 m³/s2,00022,00020,000+10%+0.196 %
U1 Inlet mean speed0.01 to 50 m/s2,0003,000999.8+10%+0.196 %
ρ Liquid density500 to 2,000 kg/m³2,0202,08060+10%+0.196 %
p2 Outlet gauge pressure1,000 to 1e8 Pa2,0402,0400+10%0 %
A2 Outlet area1e-4 to 1 m²2,0402,0400+10%0 %
U2 Outlet mean speed0.01 to 50 m/s2,0402,0400+10%0 %

Sweep of Inlet gauge pressure

Inlet gauge pressure (Pa)Force on the elbow, x-component (N)
1,00050
4,21782.17
17,780217.8
74,990789.9
316,2003,202
1,334,00013,380
5,623,00056,270
2.371e7237,200
1e81,000,000

Sweep one variable

Force on the elbow, x-component (N)Hover, touch, or use the arrow keys on the chart
0200k400k600k800k1M 100010k100k1M10M100M Inlet gauge pressure (Pa), log scale now 2,040

Variables and how each one contributes

Fx

Force on the elbow, x-component

Result · N

What the equation gives you. Everything else feeds it.

p1

Inlet gauge pressure

Pa · typical 1,000 to 1e8

The gauge pressure at the inlet, in Pa. Raises the x-force in direct proportion to the inlet area. Raising it by 10 % (to 220,000) moves the result by +9.8 %, from 2,040 to 2,240 N.

p2

Outlet gauge pressure

Pa · typical 1,000 to 1e8

The gauge pressure at the outlet, in Pa. Changes only the y-component, so the x-force is unchanged. Raising it by 10 % (to 165,000) moves the result by +0 %, from 2,040 to 2,040 N.

A1

Inlet area

m² · typical 1e-4 to 1

The inlet area, in m². Raises the pressure force on the inlet in direct proportion. Raising it by 10 % (to 0.011) moves the result by +9.8 %, from 2,040 to 2,240 N.

A2

Outlet area

m² · typical 1e-4 to 1

The outlet area, in m². Changes only the y-component, so the x-force is unchanged. Raising it by 10 % (to 0.011) moves the result by +0 %, from 2,040 to 2,040 N.

ρ

Liquid density

kg/m³ · typical 500 to 2,000

The liquid density, in kg/m³. Raises the momentum part in direct proportion. Raising it by 10 % (to 1,100) moves the result by +0.196 %, from 2,040 to 2,044 N.

Q

Discharge

m³/s · typical 1e-4 to 10

The discharge, in m³/s. Raises the momentum part in direct proportion. Raising it by 10 % (to 0.022) moves the result by +0.196 %, from 2,040 to 2,044 N.

U1

Inlet mean speed

m/s · typical 0.01 to 50

The mean speed at the inlet, in m/s. Raises the momentum part in direct proportion. Raising it by 10 % (to 2.2) moves the result by +0.196 %, from 2,040 to 2,044 N.

U2

Outlet mean speed

m/s · typical 0.01 to 50

The mean speed at the outlet, in m/s. Changes only the y-component, so the x-force is unchanged. Raising it by 10 % (to 2.2) moves the result by +0 %, from 2,040 to 2,040 N.

Worked example with the values above

  1. Pressure force at the inlet: p₁A₁ = 200,000 × 0.01 = 2,000 N.
  2. Momentum flow: ρ Q U₁ = 1,000 × 0.02 × 2 = 40 N.
  3. Fx = 2,040 N; the y-component is −1,540 N.

Assumptions and limits

  • Steady, incompressible, inviscid flow outside the boundary layer, at atmospheric pressure where stated.
  • Uniform velocity profiles at the sections used.

Common mistakes

  • Using the area of the pipe where the jet area is needed.
  • Mixing gauge and absolute pressures in a force balance.
  • Forgetting that the force on the support is the reaction to the force on the fluid.

Statistics and uncertainty

Discharge and velocity coefficients vary with the Reynolds number and with the geometry, and measured jet distances carry the reading error of the ruler, so the results are no better than 2 % to 5 %.

Where it is used

  • Timing tank drainage and calibrating nozzles and orifices.
  • Sizing thrust blocks, deflectors and jet impact plates.

Maths you need

  • Torricelli’s law: jet speed √(2gh) from a head h
  • Momentum equation: force = rate of change of momentum
  • Continuity: Q = A U

Related formulas

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