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Flow Measurement · Free Calculator

Venturi Tube Flow Calculator

Calculate flow through a classical venturi tube from its differential pressure. The discharge coefficient follows ISO 5167-4 for the chosen construction, and gases include the expansibility factor.

ISO 5167-4Liquid and gasLow pressure lossMass and volume flow
Mass flow274,380 kg/h
Volume flow (actual)274.88 m³/h
Beta ratio β0.6000
Expansibility ε1.0000
Throat velocity6.751 m/s
How this result was calculated
  1. β = 0.6000, C = 0.995
  2. qm = C ÷ √(1 − β⁴) × ε × π/4 × d² × √(2ΔPρ) = 76.218 kg/s
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Venturi Flow Equation

qm = C ÷ √(1 − β⁴) × ε × (π/4) × d² × √(2 × ΔP × ρ1)
ε = √[ κτ2/κ/(κ − 1) × (1 − β⁴)/(1 − β⁴τ2/κ) × (1 − τ(κ−1)/κ)/(1 − τ) ], τ = p2/p1

Worked example

Water through a machined venturi, D = 200 mm, d = 120 mm (β = 0.6), at 200 mbar: qm ≈ 274,000 kg/h (about 275 m³/h).

Key insight: a venturi recovers most of its DP, losing only about 5 to 20 % permanently compared with 40 to 70 % for an orifice, which saves pumping energy on large lines.
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Frequently Asked Questions

Why is the venturi discharge coefficient close to 1?

The smooth convergent section guides the flow without a vena contracta, so the actual flow is almost the theoretical flow.

When should I use a venturi instead of an orifice?

On large lines, dirty fluids or where pressure loss is costly. Venturis cost more but need less straight pipe and recover more pressure.

What is the expansibility factor for gas?

It corrects for gas expansion as pressure falls into the throat. It is 1 for liquids and slightly less than 1 for gases.

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