Flow measurement: venturi, orifice and Pitot-static tube
Venturi, orifice and Pitot-static measurement from Bernoulli and continuity, discharge coefficients and the velocity-of-approach factor, manometer conversion, and equivalent versus true airspeed.
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Why it matters
Every aircraft shows its airspeed from a Pitot-static system, every wind tunnel sets its test speed from a pressure difference, and fuel, hydraulic and coolant lines are metered with Venturis and orifice plates. All of these devices are Bernoulli plus continuity, corrected with a coefficient for real-fluid losses. Getting the coefficient, the area ratio and the manometer reading right is what separates a correct flow rate from one that is 30 % off.
Key ideas
Differential-pressure meters. A restriction speeds the flow up; continuity gives the speed ratio from the area ratio, and Bernoulli turns the speed change into a pressure drop. Measuring the pressure drop therefore gives the flow rate, with Q proportional to √Δp.
Venturi meter. A smooth converging cone (about 20°), a throat, and a long diverging diffuser (5–15°) that recovers most of the pressure. Flow stays attached, so losses are small and the discharge coefficient C_d is high (about 0.95–0.99). Permanent pressure loss is typically 10–20 % of the measured difference. Drawback: long and expensive.
Orifice meter. A thin plate with a sharp-edged hole. The jet keeps contracting downstream to a vena contracta (area ratio C_c ≈ 0.61–0.65), then expands abruptly with large losses. C_d is about 0.6–0.65 and depends on the diameter ratio β = d/D, the tapping positions and Reynolds number; take it from the standard or calibration. It is cheap and compact but wastes much more pressure. A flow nozzle sits between the two.
Coefficients. C_d = actual Q / ideal Q = C_c × C_v, where C_v (velocity coefficient, about 0.97–0.99) accounts for friction and C_c for jet contraction. The "velocity of approach" factor 1/√(1 − β⁴) corrects for the upstream velocity not being zero.
Pitot tube and Pitot-static tube. A tube facing the flow brings fluid to rest at its mouth and reads stagnation (total) pressure p₀. Side holes parallel to the flow read static pressure p. The difference is the dynamic pressure, so V = √(2(p₀ − p)/ρ) in incompressible flow. A Pitot-static probe measures velocity at a point; integrating across a duct gives flow rate. Errors come from misalignment (yaw over about 10–15°), probe blockage, turbulence and, at high speed, compressibility.
Airspeeds in aviation. The airspeed indicator is calibrated with sea-level density ρ₀ = 1.225 kg/m³, so it shows (after instrument and position corrections) equivalent airspeed V_E = √(2q/ρ₀). True airspeed is V = V_E·√(ρ₀/ρ), higher at altitude. Above about Mach 0.3 the compressible Pitot relation must be used, and in supersonic flow a bow shock forms in front of the probe (Rayleigh Pitot formula; see compressible flow).
Manometer readings. For a U-tube with manometric liquid ρ_m under a flowing fluid ρ, the pressure difference is (ρ_m − ρ)·g·h, independent of the meter's inclination when both limbs are filled with the flowing fluid.
Formulas
Q = C_d · A₁·A₂ / √(A₁² − A₂²) · √(2Δp/ρ)
- Venturi or nozzle; A₁: inlet area (m²); A₂: throat area (m²); Δp = p₁ − p₂ (Pa); ρ (kg/m³); C_d dimensionless.
Q = C_d · A₀ · √(2Δp / (ρ·(1 − β⁴)))
- Orifice; A₀: orifice area (m²); β = d/D (dimensionless).
Δp = (ρ_m − ρ)·g·h or as head h_f = h·(ρ_m/ρ − 1)
- h: manometer deflection (m); h_f: head of flowing fluid (m).
V = √(2(p₀ − p)/ρ)
- Pitot-static, incompressible; p₀: stagnation pressure (Pa); p: static pressure (Pa).
V_E = √(2q/ρ₀) and V_TAS = V_E·√(ρ₀/ρ)
- q = p₀ − p (Pa); ρ₀ = 1.225 kg/m³.
Worked examples
Example 1 (standard): Venturi with a mercury manometer. Given: water, D₁ = 200 mm, d₂ = 100 mm, mercury deflection h = 250 mm, C_d = 0.98.
- Areas: A₁ = 0.031416 m², A₂ = 0.0078540 m².
- Head difference in water:
h_f = h(ρ_m/ρ − 1)= 0.25 × 12.6 = 3.15 m. - Ideal:
Q = A₁A₂/√(A₁² − A₂²) · √(2g·h_f)= 0.0081118 × √(61.803) = 0.06377 m³/s. - Actual: 0.98 × 0.06377 = 0.06249 m³/s. Answer: Q ≈ 0.0625 m³/s (62.5 L/s).
Example 2 (standard): orifice plate. Given: water, D = 200 mm, orifice d = 100 mm (β = 0.5), C_d = 0.62 (from the standard), Δp = 20 kPa.
- A₀ = 0.0078540 m², 1 − β⁴ = 0.9375.
Q = C_d·A₀·√(2Δp/(ρ(1 − β⁴)))= 0.62 × 0.0078540 × √(40 000/937.5) = 0.62 × 0.0078540 × 6.532. Answer: Q ≈ 0.0318 m³/s.
Example 3 (GATE level): airspeed. (a) A Pitot-static tube in a wind tunnel (air ρ = 1.2 kg/m³) is connected to a water U-tube reading 50 mm.
- Δp = (ρ_w − ρ_air)gh ≈ 1000 × 9.81 × 0.05 = 490.5 Pa (air column negligible).
- V = √(2 × 490.5/1.2) = 28.6 m/s. (b) An aircraft's Pitot-static system measures q = 2000 Pa at an altitude where ρ = 0.9093 kg/m³.
- Equivalent airspeed
V_E = √(2q/ρ₀)= √(4000/1.225) = 57.1 m/s. - True airspeed
V = √(2q/ρ)= √(4000/0.9093) = 66.3 m/s. Answer: V_E ≈ 57.1 m/s, V_TAS ≈ 66.3 m/s.
Common mistakes
- Forgetting the area-ratio factor A₁/√(A₁² − A₂²) (the velocity of approach) and using Q = A₂√(2Δp/ρ).
- Using h of mercury directly as a head of water. Convert with (ρ_m/ρ − 1), not ρ_m/ρ.
- Using C_d of a Venturi (≈ 0.98) for an orifice (≈ 0.6), or omitting C_d altogether.
- Using sea-level density at altitude when true airspeed is wanted.
- Using incompressible Pitot relations at high subsonic or supersonic speed.
- Unit slips between mm and m and between diameters and areas.
For GATE AE
Expect Pitot-static airspeed with a manometer reading, equivalent versus true airspeed at a given altitude, Venturi and orifice discharge with C_d, manometer conversion to head, and conceptual MCQs on why Venturis have lower permanent loss and where the vena contracta forms. Practise the full Venturi formula until it is automatic, and keep the ISA density table in mind.
Quick check
- Air (ρ = 1.2 kg/m³), p₀ − p = 200 Pa. What is V?
- A mercury–water manometer reads 100 mm. What is the head of water?
- Which meter has the larger permanent pressure loss for the same flow and area ratio, Venturi or orifice?
- q = 1500 Pa at sea level. What is V?
Answers: 1. 18.3 m/s 2. 1.26 m 3. Orifice 4. 49.5 m/s
Interview questions
All Fluid Mechanics interview questionsTry answering each one aloud before you open it.
1.What is a Venturi meter and how does it work?Concept
A Venturi meter is a device used to measure the flow rate of fluid in a pipe. It works on the principle of Bernoulli's equation, which relates the pressure, velocity, and height of a fluid. The Venturi meter consists of a converging section, a throat, and a diverging section. As fluid flows through the converging section, its velocity increases and pressure decreases. At the throat, the velocity is at its maximum and pressure is at its minimum. The pressure difference between the inlet and the throat is used to calculate the flow rate.
2.Explain the working principle of an orifice plate.Concept
An orifice plate is a thin plate with a hole in the middle, used to measure flow rate. It works on the principle of differential pressure measurement. As fluid passes through the orifice, it experiences a drop in pressure. The pressure difference between the upstream side and the downstream side of the orifice is proportional to the square of the flow rate. By measuring this pressure difference, the flow rate can be determined.
3.What is a Pitot-static tube and how is it used to measure fluid flow?Concept
A Pitot-static tube is a device used to measure fluid flow velocity. It consists of two tubes: a Pitot tube that measures the total pressure (static plus dynamic) and a static tube that measures the static pressure. The difference between these pressures gives the dynamic pressure, which can be used to calculate the fluid velocity using Bernoulli's equation. This method is commonly used in aviation to measure airspeed.
4.Why is a Venturi meter preferred over an orifice plate in some applications?Application
A Venturi meter is preferred over an orifice plate in applications where energy loss needs to be minimized. The Venturi meter has a gradual converging and diverging section, which results in lower energy losses compared to the sudden contraction and expansion in an orifice plate. This makes the Venturi meter more efficient and suitable for applications where maintaining pressure is critical.
5.What happens if the throat of a Venturi meter is blocked?Application
If the throat of a Venturi meter is blocked, the flow of fluid through the meter will be obstructed, leading to a significant increase in pressure upstream of the blockage. This will prevent accurate measurement of the flow rate, as the pressure difference between the inlet and the throat will not reflect the actual flow conditions. It may also cause damage to the system due to increased pressure.
6.How does the presence of air bubbles affect the accuracy of an orifice plate measurement?Application
The presence of air bubbles in the fluid can affect the accuracy of an orifice plate measurement by altering the density and flow characteristics of the fluid. Air bubbles can cause fluctuations in the pressure readings, leading to errors in the calculated flow rate. It is important to ensure that the fluid is free of air bubbles for accurate measurements.
7.Calculate the ideal flow rate through a Venturi meter with an inlet diameter of 0.1 m, a throat diameter of 0.05 m, and a pressure difference of 500 Pa. Assume the fluid density is 1000 kg/m³.Numerical
Q = A₁A₂/√(A₁² − A₂²) · √(2Δp/ρ). A₁ = π(0.1)²/4 = 7.854×10⁻³ m² and A₂ = 1.963×10⁻³ m², so A₁A₂/√(A₁² − A₂²) = A₂/√(1 − (A₂/A₁)²) = 1.963×10⁻³/√(1 − 1/16) = 2.028×10⁻³ m². √(2 × 500/1000) = 1 m/s, so Q ≈ 2.03×10⁻³ m³/s (about 2 L/s). The actual flow is C_d times this, about 0.98 × 2.03 ≈ 1.99 L/s.
8.Determine the velocity of air using a Pitot-static tube if the dynamic pressure is 250 Pa and the air density is 1.225 kg/m³.Numerical
The velocity can be calculated using the equation: v = √(2 * ΔP / ρ), where ΔP is the dynamic pressure and ρ is the air density. v = √(2 * 250 / 1.225) = √(408.16) = 20.2 m/s.
9.How well does a Pitot-static tube work in turbulent flow?Application
Pitot-static tubes are routinely used in turbulent pipe and wind-tunnel flows; with pneumatic damping they give the time-averaged dynamic pressure and hence the mean velocity. The errors are that the reading is the average of ½ρu² rather than ½ρū², so strong turbulence makes it read a few per cent high, and large angle fluctuations add yaw error. For the fluctuating velocity itself you need a fast sensor such as a hot-wire anemometer or LDV.
10.What are the limitations of using an orifice plate for flow measurement?Application
The limitations of using an orifice plate for flow measurement include high energy losses due to the sudden contraction and expansion of the fluid, potential for clogging if the fluid contains particulates, and sensitivity to changes in fluid density and viscosity. Additionally, orifice plates can cause significant pressure drops, which may not be acceptable in systems where maintaining pressure is important.
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