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Hydraulics, open channels and fluid power

Outlet whirl velocity from the impeller velocity triangle

Tangential component of the absolute velocity leaving the impeller, from the tip speed U₂, the outward meridional velocity Vm and the blade angle β measured from the backward tangent (degrees), for ideal blade-guided flow.

Ref
HYD-40
Rev
v1
Field
Hydraulics, open channels and fluid power
Result
Vθ2 [m/s]

In the exit velocity triangle, the absolute tangential component is the blade speed less the relative velocity’s tangential part: Vθ₂ = U₂ − Vm₂ cot β₂, where Vm₂ is the radial (meridional) velocity and β₂ the blade angle from the backward tangent. With a radial blade (β₂ = 90°) Vθ₂ = U₂, and backward-leaning blades give less. Real flow has slip, so the whirl is less than this ideal value.

Tangential component of the absolute velocity leaving the impeller, from the tip speed U₂, the outward meridional velocity Vm and the blade angle β measured from the backward tangent (degrees), for ideal blade-guided flow.

Calculator

Solve for
m/s
m/s
1200
m/s
050
°
5175
  • Head coefficient, Vθ₂/U₂0.8
  • Euler head with no inlet whirl, U₂Vθ₂/9.8132.62 m
  • Absolute exit speed, √(Vθ₂² + Vm²)16.49 m/s

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.

Outlet whirl velocity (m/s) current value 16 m/s
U2Blade tip speedKey driver
−3196
βBlade angle from the backward tangent
−25.765.7
VmOutward meridional velocity
−3020
  • With a tip speed of 20 m/s and 4 m/s of radial flow, the exit whirl is 16 m/s, 80 % of the tip speed.
  • Higher flow gives a lower whirl and so a lower head, which is the falling pump curve of a backward-curved impeller.
Chart data as tables

Ranked variables

VariableTypical rangeLowest resultHighest resultSwing (m/s)Local stepChange in result
U2 Blade tip speed1 to 200 m/s−3196199+10%+12.5 %
β Blade angle from the backward tangent5 to 175 °−25.7265.7291.44+10%+3.65 %
Vm Outward meridional velocity0 to 50 m/s−302050+10%−2.5 %

Sweep of Blade angle from the backward tangent

Blade angle from the backward tangent (°)Outlet whirl velocity (m/s)
5−25.72
26.2511.89
47.516.33
68.7518.44
9020
111.321.56
132.523.67
153.828.11
17565.72

Sweep one variable

Outlet whirl velocity (m/s)Hover, touch, or use the arrow keys on the chart
−200204060 2060100140 Blade angle from the backward tangent (°) now 16

Variables and how each one contributes

Vθ2

Outlet whirl velocity

Result · m/s

What the equation gives you. Everything else feeds it.

U2

Blade tip speed

m/s · typical 1 to 200

The blade tip speed, in m/s. Raises the whirl in direct proportion. Raising it by 10 % (to 22) moves the result by +12.5 %, from 16 to 18 m/s.

Vm

Outward meridional velocity

m/s · typical 0 to 50

The outward meridional velocity, in m/s. More flow lowers the whirl, so the head falls with flow. Raising it by 10 % (to 4.4) moves the result by −2.5 %, from 16 to 15.6 m/s.

β

Blade angle from the backward tangent

° · typical 5 to 175

The blade angle from the backward tangent, in degrees. A more radial blade (larger angle) raises the whirl. Raising it by 10 % (to 49.5) moves the result by +3.65 %, from 16 to 16.58 m/s.

Worked example with the values above

  1. Cotangent: cot 45° = 1 / tan 45° = 1.
  2. Flow term: Vm cot β = 4 × 1 = 4 m/s.
  3. Vθ₂ = 20 − 4 = 16 m/s.

Assumptions and limits

  • Steady incompressible flow with the pump curve and system curve both of quadratic form.
  • Ideal blade-guided flow for the velocity-triangle results, so the real head is lower.

Common mistakes

  • Measuring the blade angle from the tangent in the forward direction in place of the backward tangent.
  • Forgetting that the real whirl is lowered by slip.
  • Using degrees in a calculator set to radians.

Statistics and uncertainty

Pump curves are known only to within a few percent and wear them down in service, and available suction head changes with the level, temperature and flow, so use a safety margin on the requirement.

Where it is used

  • Choosing pumps and finding the duty point on a pipe system.
  • Checking cavitation margin and estimating head from impeller geometry.

Maths you need

  • Pump curve: head against flow for a pump at a fixed speed
  • System curve: head needed by the pipe system against flow
  • Velocity triangle: the vector diagram of blade and fluid velocities

Related formulas

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