If you need any help, please feel free to contact us
A Vortex Flowmeter measures fluid flow by detecting the frequency of vortices shed by a bluff body (shedder bar) placed in the flow stream, with that frequency being directly and linearly proportional to the fluid velocity according to the Strouhal relationship. The insertion vortex flow meter is a probe-style variant inserted through a tapping in the pipe wall rather than inline, making it ideal for large-diameter pipes where full-bore meters would be prohibitively expensive. A vortex air flow meter measures compressed air, HVAC air flows, and combustion air with accuracy typically of ±1.0% to ±1.5% of reading. The vortex flow meter for steam application is one of the most important uses in process industry because steam is difficult to measure accurately with differential pressure devices, and vortex meters handle both saturated and superheated steam reliably at temperatures up to 400°C and pressures up to 40 bar. A vortex type flow transmitter integrates the sensor, signal conditioning, and output transmission (4 to 20 mA, HART, Modbus, FOUNDATION Fieldbus, or pulse) into a single compact housing mounted on the meter body. This guide covers every practical dimension of vortex flowmeter selection, installation, and application.
What is vortex flow in the context of flow measurement? It refers to the phenomenon of vortex shedding, a fluid mechanics effect that occurs when a fluid stream encounters a bluff (non-streamlined) body. The flowing fluid cannot follow the sharp contours of the bluff body, separates from its surface, and forms alternating clockwise and counter-clockwise vortices that are shed from the two sides of the body in a regular, repeating pattern. This pattern of alternating vortices is called the Karman vortex street, named after the Hungarian-American physicist Theodore von Kármán who mathematically characterized the phenomenon in the early twentieth century.
The key physical relationship that makes vortex shedding useful for flow measurement is the Strouhal relationship. For a given bluff body geometry in a given pipe, the ratio of the vortex shedding frequency (f) to the fluid velocity (V) divided by the characteristic dimension of the bluff body (d) is a dimensionless constant called the Strouhal number (St):
St = f × d ÷ V
For well-designed vortex flowmeter bluff bodies, the Strouhal number is constant over a Reynolds number range of approximately 10,000 to 4,000,000, meaning the shedding frequency is strictly proportional to velocity across this wide range. Rearranging the Strouhal relationship gives:
f = St × V ÷ d
Since St and d are fixed for a given meter body, measuring the frequency f directly gives the velocity V, and multiplying by the known pipe cross-sectional area gives the volumetric flow rate. This is the entire operating principle of a Vortex Flowmeter: count vortices, compute velocity, calculate volume. The meter's K-factor (pulses per unit volume) encodes the combined Strouhal number and pipe geometry into a single calibration constant that converts raw pulse count to flow rate in the transmitter electronics.
The alternating pressure fluctuations created by shedded vortices are small (typically 0.1 to 10% of the line pressure) but measurable. Commercial Vortex Flowmeter designs use several sensor technologies to detect these pressure fluctuations:
The Strouhal relationship holds only above a minimum Reynolds number, typically Re greater than 10,000 to 20,000 depending on the specific meter design. Below this threshold, vortex shedding becomes irregular and non-periodic, making accurate flow measurement impossible. This defines the minimum measurable flow rate for a given fluid in a given meter size. The minimum velocity required to maintain Re above 10,000 depends on the fluid's kinematic viscosity: for water at 20°C this is approximately 0.3 to 0.5 m/s, while for viscous oils (above 10 cSt) it may be significantly higher. This Reynolds number limitation is the primary reason vortex flowmeters are not suitable for high-viscosity fluid applications.
The insertion vortex flow meter is a probe-style instrument designed to be inserted through a single tapping in the pipe wall rather than installed inline as a full-bore spool piece. The probe extends into the pipe cross-section to a depth where it samples flow velocity at a specific point, and this point velocity is used to calculate the mean velocity and volumetric flow rate of the entire pipe cross-section through a calibrated velocity-to-flow relationship. Insertion vortex meters are the dominant choice for pipes above approximately DN 200 (8 inch) where full-bore vortex meters become very expensive and heavy.
A typical insertion vortex flow meter consists of:
The accuracy of an insertion vortex flow meter depends critically on knowing the relationship between the velocity at the insertion point and the mean velocity across the entire pipe cross-section. This relationship is the velocity profile factor (also called the meter factor or insertion factor). For a fully developed turbulent pipe flow profile, the ratio of centerline velocity to mean velocity is approximately 1.2 to 1.25, meaning the centerline velocity is 20 to 25% higher than the mean. When the probe is inserted to the centerline, the measured velocity must therefore be divided by this factor to get the mean velocity. The velocity profile factor is influenced by:
| Criterion | Insertion Vortex Flow Meter | Full-Bore Inline Vortex Flowmeter |
|---|---|---|
| Pipe size range | DN 50 to DN 2000 and above | DN 15 to DN 300 (typical) |
| Typical accuracy | ±1.5 to ±3.0% of reading | ±0.5 to ±1.0% of reading |
| Installation | Single pipe tapping; hot-tap capable | Requires pipe section removal and flanged spool |
| Pressure drop | Very low (probe only) | Moderate (shedder body across full bore) |
| Cost (DN 300 pipe) | Low to moderate | High (large flanged body) |
| Straight pipe requirement | 15 to 30D upstream, 5D downstream | 10 to 20D upstream, 5D downstream |
| Best application | Large pipes, retrofit, air and gas | Small to medium pipes, high accuracy |
A vortex air flow meter is one of the most practical instruments for measuring air flow in industrial, commercial, and HVAC applications. Air presents both advantages and challenges for vortex flow measurement: its low density means low vortex-induced pressure fluctuations (requiring sensitive detection), but its low viscosity means the Reynolds number is typically well above the 10,000 threshold for vortex shedding even at moderate velocities in standard pipe sizes.
Compressed air systems in manufacturing facilities typically operate at 6 to 10 bar gauge pressure. Measuring compressed air consumption accurately is essential for energy auditing, leak detection, and allocating air costs to production processes. Vortex flowmeters are well-suited to compressed air measurement because:
For HVAC duct air flow measurement at or near atmospheric pressure, insertion vortex flow meters are particularly popular because HVAC ductwork is typically large (DN 200 to DN 1000 and above) and rectangular or circular sheet metal construction where a full-bore meter cannot be installed. The probe-style insertion meter is installed through a single hole drilled in the duct wall, requiring no duct section replacement. Key HVAC vortex application considerations:
Vortex air flow meters are used for combustion air flow measurement in industrial burner systems, boilers, and kilns where the ratio of air to fuel (the air-fuel ratio) must be controlled precisely for combustion efficiency and emissions compliance. In these applications, the vortex air flow meter output feeds directly into the burner management system or combustion controller. The meter must be rated for the elevated air temperatures typically seen in combustion air preheating systems: industrial combustion air preheat temperatures of 200 to 400°C are common, and the meter must be specified with high-temperature wetted materials and temperature-compensated electronics.
The vortex flow meter for steam application is one of the most technically important and commercially significant uses of vortex technology. Steam flow measurement has historically been dominated by differential pressure (DP) meters with orifice plates, but the superior accuracy, lower maintenance, and direct mass flow capability of vortex meters have made them the preferred choice for steam applications in modern process plants and utility systems.
Steam measurement is challenging for several reasons that make many flow measurement technologies unsuitable:
Vortex flowmeters handle both saturated and superheated steam, but the measurement approach and required ancillary measurements differ:
For steam service, vortex flowmeter body and internal components must meet specific material requirements:
| Parameter | Saturated Steam | Superheated Steam |
|---|---|---|
| Pressure range | 0.5 to 25 bar absolute | 1 to 40 bar absolute |
| Temperature range | 100°C to 225°C | 120°C to 400°C |
| Required measurements | Velocity + P (or T) | Velocity + T + P |
| Volumetric accuracy | ±1.0% of reading | ±1.0% of reading |
| Mass flow accuracy | ±1.5 to ±2.0% | ±1.5 to ±2.5% |
| Body material | Carbon steel or SS316 | SS316 or alloy steel |
| Transmitter type | Multivariable (P compensation) | Multivariable (T and P compensation) |
A vortex type flow transmitter is the electronic module that accepts the raw vortex pulse signal from the sensor (piezoelectric, capacitive, or ultrasonic), processes it through signal conditioning and filtering algorithms, calculates the flow rate, and transmits the result to the control system or data acquisition system through one or more standardized output signals. In modern instruments, the transmitter is physically integrated into the meter body rather than being a separate remote-mount device, giving the compact assembly its "smart transmitter" designation.
The raw signal from a vortex sensor is a low-amplitude alternating signal whose frequency represents the vortex shedding rate. In process environments, this signal is contaminated by several sources of interference that the vortex type flow transmitter must reject:
A vortex type flow transmitter provides one or more of the following output signals, depending on the model and configuration:
The multivariable vortex type flow transmitter integrates temperature measurement (RTD or thermocouple), pressure measurement (integrated pressure transducer), and flow measurement (vortex sensor) into a single instrument package. The transmitter calculates fluid density in real time from the measured temperature and pressure using built-in equations of state for steam, natural gas, air, and other common process fluids, then multiplies the volumetric flow by the calculated density to output mass flow directly. Key benefits of multivariable transmitters:
Correct installation is the single most important factor determining whether a Vortex Flowmeter achieves its specified accuracy in service. Even the best-calibrated meter will give poor results if installed without adequate upstream straight pipe, in an orientation that traps gas or liquid in the wrong location, or without attention to process connections.
Vortex flowmeters require a fully developed, undistorted velocity profile to achieve their calibrated accuracy. Upstream piping disturbances (bends, valves, expanders, reducers) distort the profile and introduce systematic error. Minimum straight pipe requirements (D = pipe internal diameter):
When these straight pipe requirements cannot be met due to space constraints, a flow conditioner (such as a tube bundle, perforated plate, or CPA 50E-type conditioner) installed immediately upstream of the meter can reduce the required straight pipe run to 10D or less by homogenizing the flow profile before it reaches the meter.
Vortex Flowmeters can be installed in horizontal, vertical, or inclined pipes, but the mounting orientation of the transmitter and the flow direction relative to gravity must be considered:
What is vortex flow in measurement terms? It is the phenomenon of Karman vortex shedding: when a fluid flows past a bluff body (shedder bar), alternating vortices are shed from each side of the body in a regular pattern. The shedding frequency is directly proportional to the fluid velocity through the Strouhal relationship (f = St × V ÷ d). A Vortex Flowmeter counts this frequency using a piezoelectric or capacitive sensor, converts frequency to velocity, multiplies by pipe area, and outputs volumetric or mass flow rate. The Strouhal number remains constant for Reynolds numbers above approximately 10,000 to 4,000,000, giving linear measurement across this wide range.
An insertion vortex flow meter offers significant cost advantages for large-diameter pipes where a full-bore inline meter would require large, heavy, expensive flanged spool pieces. The insertion meter uses a single pipe tapping, can be hot-tapped (installed without process shutdown on pressurized systems), creates very low pressure drop (probe only, not full bore), and handles pipe sizes from DN 50 to DN 2000 and above with the same compact probe design. The tradeoff is accuracy: insertion meters typically achieve ±1.5 to ±3.0% of reading versus ±0.5 to ±1.0% for full-bore designs, because point velocity measurement introduces additional uncertainty from the velocity profile assumption.
Yes. A vortex air flow meter with integrated temperature and pressure compensation is ideal for compressed air energy accounting. The multivariable transmitter converts line volumetric flow to standard volumetric flow (referenced to defined standard conditions) or directly to mass flow, which is what determines the compressor energy consumed. The vortex meter's high turndown ratio (20:1 to 40:1) handles the wide variation in compressed air demand across shifts and production states, and its no-moving-parts design is well-suited to compressed air that may contain entrained oil or moisture.
A vortex flow meter for steam application outperforms a traditional orifice plate differential pressure meter in steam service for several reasons: it delivers higher accuracy (±1.0% of reading vs. ±2 to ±3% for a typical orifice installation), provides a much wider rangeability (20:1 to 30:1 vs. 3:1 to 5:1 for DP), requires no impulse lines that can plug or freeze, has no thin orifice plate that erodes under steam, and in its multivariable form provides direct mass flow output without a separate flow computer. The vortex meter also handles condensate slugs better than DP meters with wet legs.
A vortex type flow transmitter typically provides a 4 to 20 mA analog output representing flow rate, a pulse or frequency output for totalization, and digital communication via HART protocol (the most common), FOUNDATION Fieldbus, PROFIBUS PA, or Modbus RTU/TCP depending on the model. Multivariable transmitters may provide multiple 4 to 20 mA outputs or transmit all variables (flow, temperature, pressure, density, mass flow) over a single digital fieldbus connection. The pulse output is particularly important for custody transfer and batch control applications where an integrating counter of actual fluid volume rather than an instantaneous rate signal is required.
The same physical vortex meter body can measure both gases and liquids because the Strouhal relationship is valid for any fluid above the minimum Reynolds number threshold. However, the meter must be correctly sized for each fluid (velocity range requirements differ significantly between gases and liquids due to density differences), and the transmitter must be configured with the correct fluid properties for each service. In practice, a meter sized for a gas application is typically too large for a liquid application in the same pipe because liquid requires much lower velocities for the same mass flow. Most users specify separate meters for gas and liquid service rather than attempting to use the same meter for both.
The minimum measurable flow rate of a Vortex Flowmeter is determined by the Reynolds number threshold for stable vortex shedding, typically Re > 10,000 to 20,000 depending on the meter design. For water at 20°C in a DN 50 meter, this corresponds to a minimum velocity of approximately 0.3 to 0.5 m/s and a minimum flow rate of approximately 0.3 to 0.6 m³/h. For gases and steam, the minimum velocity may be 1 to 3 m/s due to the lower Reynolds numbers per unit velocity in low-density fluids. The manufacturer's sizing software should always be used to confirm minimum flow capability for the specific fluid, temperature, pressure, and pipe size.
Upstream straight pipe requirements for a Vortex Flowmeter range from 10D to 50D depending on the upstream disturbance type. A single 90-degree bend requires a minimum of 15D; two out-of-plane bends require 25D; a control valve at partial opening requires 30D to 50D. Downstream, a minimum of 5D is required before any fitting or valve. When installation space is insufficient, a flow conditioner reduces the upstream requirement to approximately 10D regardless of the upstream configuration. The insertion vortex flow meter typically requires more upstream straight pipe than full-bore meters (15D to 30D) because the point velocity measurement is more sensitive to profile distortion.
Vortex Flowmeters are not suitable for: high-viscosity fluids (above approximately 10 to 20 cSt at operating temperature) where the Reynolds number cannot be maintained above 10,000 at practical flow velocities; slurries and fluids with high solids content that could erode the shedder bar or deposit on the sensor; multiphase flows where liquid and gas are simultaneously present in significant quantities (wet steam with quality below approximately 0.8, or liquid with more than approximately 2% gas by volume); pulsating flows where the pulsation frequency overlaps the expected vortex frequency range; and very low flow rates in small pipes where the required minimum velocity cannot be achieved without exceeding the maximum acceptable pressure drop.
Sizing a vortex flow meter for steam application requires knowing the minimum and maximum mass flow rates, the steam pressure and temperature at the measurement point, and the pipe size. From the mass flow and steam density (calculated from pressure and temperature using steam tables), the volumetric flow and velocity are determined. The meter size is selected so that the minimum flow velocity exceeds the meter's minimum velocity for stable vortex shedding (typically 1.5 to 2.5 m/s for steam) and the maximum flow velocity does not exceed the meter's rated maximum (typically 50 to 80 m/s for steam). The resulting velocity range defines the meter's turndown in service. Most manufacturers provide sizing software or online tools that perform this calculation automatically when supplied with the steam conditions and flow range.