— A Practical Guide for Engineers, EPCs, and Project Teams
Vortex flowmeters are among the most versatile flow measurement technologies in the process industries. They measure steam, gas, and low-viscosity liquids with a single device, have no moving parts, and offer wide turndown and low pressure loss. Yet the same versatility that makes them attractive also makes them easy to misapply. A vortex flowmeter sized for one medium can be completely unsuitable for another. A meter that works perfectly on compressed air can fail on saturated steam. A meter installed without proper straight pipe runs can produce errors that no amount of calibration will correct.
This guide explains how to select vortex flowmeters for steam, gas, and liquid applications—covering the principles of operation, the medium-specific considerations that drive selection, sizing calculations, installation requirements, and the common mistakes that lead to poor performance.
1. How Vortex Flowmeters Work
The vortex flowmeter operates on the Kármán vortex street principle. A bluff body (also called a vortex shedder) is placed in the flow stream. As fluid passes around the bluff body, alternating vortices are shed from each side. The frequency of vortex shedding is directly proportional to the flow velocity:
Where:
= vortex shedding frequency
= Strouhal number (a dimensionless constant for a given bluff body geometry)
= fluid velocity
= bluff body width
A piezoelectric or capacitive sensor detects the pressure pulses generated by the vortices. The flowmeter converts this frequency into a flow rate.
The critical insight: The Strouhal number is constant only within a specific Reynolds number range—typically Re > 10,000 (some sources state Re > 20,000 for optimal linearity)-. Below this threshold, the relationship between shedding frequency and velocity becomes non-linear, and measurement accuracy degrades significantly.
2. The Medium Matters: Steam, Gas, and Liquid Are Not Interchangeable
The three media categories—steam, gas, and liquid—impose fundamentally different requirements on vortex flowmeter selection. Understanding these differences is the foundation of correct selection.
2.1 Steam: The Most Demanding Application
Steam is the most challenging medium for vortex flowmeters because its density varies dramatically with both temperature and pressure.
Saturated steam: Density depends on either temperature or pressure (they are directly related). A temperature-compensated vortex flowmeter with a built-in Pt100 sensor and a saturated steam density table can automatically correct for density changes-.
Superheated steam: Density depends on both temperature and pressure. This requires both temperature and pressure compensation—either through an integrated multivariable transmitter or through external pressure and temperature inputs.
Why compensation is mandatory: Without compensation, a vortex flowmeter measures volumetric flow at actual conditions. Steam volumetric flow changes dramatically with pressure and temperature, even when the mass flow rate is constant. A 10% pressure variation can cause a 10% error in mass flow calculation if not compensated-2.
Key accuracy figures:
Volumetric flow (steam, gas): ±1.0% of reading-
Mass flow (saturated steam, temperature-compensated): ±1.7% of reading
Mass flow (saturated steam, temperature/pressure compensated): ±1.5% of reading-
Wet steam consideration: Wet steam containing less than 2% water droplets by mass is considered dry saturated steam. Beyond this threshold, the liquid droplets can cause signal noise and measurement errors. Vortex flowmeters are generally not suitable for wet steam with significant liquid content-52.
2.2 Gas: Density Compensation and Standard Condition Conversion
Gas flow measurement with vortex flowmeters requires careful attention to density and standard condition conversion.
Key considerations:
Pressure effect: Gas density is directly proportional to absolute pressure. A change in line pressure changes the volumetric flow rate even when mass flow remains constant.
Temperature effect: Gas density is inversely proportional to absolute temperature.
Standard condition conversion: Most gas flow measurements are reported at standard conditions (e.g., 0°C, 1 atm or 15°C, 1 atm). This requires converting actual volumetric flow to standard volumetric flow using the ideal gas law or a compressibility factor.
Temperature and pressure compensation is mandatory for gas flow measurement. The vortex flowmeter must either integrate pressure and temperature sensors (multivariable) or accept external inputs from separate transmitters.
Accuracy: ±1.0% to ±1.5% of reading for volumetric flow, depending on whether compensation is applied-.
Minimum velocity requirement: Gas applications require a minimum flow velocity to generate measurable vortices—typically 5 m/s or higher-2.
2.3 Liquid: The Simplest Application (with Caveats)
Liquid flow measurement is the most straightforward vortex application because liquid density varies little with temperature and pressure (unless the temperature is near the boiling point).
Key considerations:
Viscosity: Vortex flowmeters are suitable for low-viscosity liquids (typically < 20 mPa·s). High-viscosity liquids dampen vortex formation and reduce measurement accuracy-.
Minimum velocity: Liquid applications typically require a minimum velocity of 0.5 m/s to generate stable vortices-2.
Vapour pressure: For liquids near their boiling point, flashing or cavitation can occur across the bluff body. This must be evaluated during selection.
Accuracy: ±0.7% to ±0.75% of reading for liquids-.
Reynolds number: As with gas and steam, the Reynolds number must exceed 10,000 for linear operation. For high-viscosity liquids, this may require a smaller meter size to maintain the required Reynolds number at low flows.
3. Step-by-Step Selection Process
Step 1: Define the Medium and Its Properties
| Property | Why It Matters |
|---|---|
| Medium type | Steam (saturated/superheated), gas, or liquid—determines compensation requirements |
| Density at operating conditions | Determines the relationship between volumetric and mass flow; critical for sizing |
| Viscosity | High viscosity reduces vortex signal strength; limits low-flow accuracy |
| Temperature and pressure | Determines density, required compensation, and material selection |
| Cleanliness | Solids or bubbles interfere with vortex formation; may require alternative technology |
Step 2: Determine the Flow Range
The single most common selection error is sizing based on pipe diameter rather than flow range.
| Parameter | Recommendation |
|---|---|
| Normal flow rate | Should fall within 50–70% of the meter's calibrated range-2 |
| Minimum flow rate | Must be above the meter's minimum measurable velocity |
| Maximum flow rate | Must be below the meter's maximum velocity |
| Turndown required | Ratio of maximum to minimum flow; determines meter size and technology |
Turndown expectations:
Gas and steam: Better than 20:1 with proper sizing-
Low-viscosity liquids: Better than 10:1-
Theoretical maximum: 1:100, but practical limits are lower due to low-flow signal-to-noise issues-
Why sizing matters: If the normal flow rate is only 10% of the meter's range, the vortex signal may be too weak to detect reliably. If the flow rate exceeds 80% of range, the pressure loss becomes excessive and the meter may be damaged by erosion. The solution is often to select a meter smaller than the pipe size—typically one or two sizes smaller—to increase velocity through the meter-.
Step 3: Calculate the Required Meter Size
The meter size is determined by the flow range, not the pipe size. The following steps apply:
Calculate the expected velocity for the minimum and maximum flow rates using the pipe inside diameter.
Compare with the meter's velocity range:
Liquid: Typically 0.5–6 m/s (some sources allow up to 10 m/s)-37
Gas: Typically 5–60 m/s-37
Steam: Typically 7–50 m/s (saturated) and 7–70 m/s (superheated)-37
If the velocity is below the minimum, select a smaller meter size.
If the velocity is above the maximum, select a larger meter size.
Verify the Reynolds number exceeds 10,000 at the minimum flow rate.
Sizing example: A gas line with a DN100 pipe and a flow range of 100–800 Nm³/h. The normal operating pressure is 5 bar(g) and the temperature is 30°C. Calculate the actual volumetric flow at operating conditions, then calculate the velocity in DN100 pipe. If the velocity at minimum flow is below 5 m/s, consider a DN80 or DN50 meter to increase velocity.
Step 4: Select Compensation Requirements
| Medium | Required Compensation |
|---|---|
| Saturated steam | Temperature or pressure compensation (one is sufficient)- |
| Superheated steam | Both temperature and pressure compensation- |
| Gas | Both temperature and pressure compensation |
| Liquid | Generally not required (unless near boiling point) |
Implementation options:
Integrated multivariable vortex flowmeter: The meter includes temperature and pressure sensors and calculates compensated mass flow internally.
External compensation: Separate temperature and pressure transmitters feed a flow computer or DCS, which performs the compensation calculation.
Best practice: For steam and gas applications, integrated multivariable vortex flowmeters are preferred because they eliminate wiring complexity, reduce installation cost, and ensure that compensation is always correctly applied.
Step 5: Select Construction and Materials
| Selection Factor | Options |
|---|---|
| Body material | Carbon steel (economical), 316L stainless steel (general), Hastelloy (corrosive) |
| Sensor type | Piezoelectric (general), capacitive (better vibration immunity) |
| Process connection | Flanged (mainstream), wafer (compact), threaded (high pressure) |
| Temperature rating | Standard up to 240°C; high-temperature models up to 400°C-2 |
| Pressure rating | PN16, PN25, PN40, PN63, PN100, or higher |
| Ex certification | Ex d IIC T6 or Ex ia IIC T6 for hazardous areas |
| Ingress protection | IP65 minimum; IP67 for outdoor or washdown |
Step 6: Verify Installation Requirements
Vortex flowmeters are sensitive to flow disturbances. The installation location must provide sufficient straight pipe runs to ensure a fully developed velocity profile.
Minimum straight pipe requirements (per ISO 12764 and manufacturer recommendations):
| Upstream Condition | Required Upstream Length | Required Downstream Length |
|---|---|---|
| General (no fittings) | 10D | 5D-26 |
| Single 90° elbow | 20D | 5D |
| Two 90° elbows in same plane | 25D | 5D |
| Two 90° elbows in different planes | 40D | 5D-26 |
| Fully open gate valve | 10D | 5D-26 |
| Partially open valve | 20D or more | 5D- |
| Reducer | 5D | 5D- |
Key principles:
Install upstream of valves and fittings wherever possible-.
Install in horizontal pipe with the sensor on top for liquid service to prevent gas pockets.
Avoid vertical downward flow for gas and steam; liquid service can use vertical upward flow.
Ensure concentric alignment between the meter and the pipe; eccentric installation causes uneven flow distribution-26.
Support the pipe upstream and downstream to prevent vibration transmission-26.
4. Common Applications and Selection Examples
Example 1: Saturated Steam Header
Application: Measure saturated steam flow in a DN80 header. Pressure: 8 bar(g), temperature: 175°C. Flow range: 200–1,500 kg/h.
Selection:
Medium: Saturated steam → temperature compensation sufficient
Meter: Integrated multivariable vortex flowmeter with Pt100 sensor
Size: Calculate velocity at minimum and maximum flow. If velocity at 200 kg/h is below 7 m/s in DN80, consider DN50 meter
Compensation: Temperature compensation with saturated steam density table
Output: 4–20 mA + HART for mass flow
Example 2: Compressed Air
Application: Measure compressed air in a DN50 pipe. Pressure: 7 bar(g), temperature: 35°C. Flow range: 50–400 Nm³/h.
Selection:
Medium: Gas → temperature and pressure compensation required
Meter: Multivariable vortex flowmeter with integrated pressure and temperature sensors
Size: Convert Nm³/h to actual m³/h at operating conditions. Calculate velocity. Ensure minimum velocity exceeds 5 m/s
Compensation: Both temperature and pressure
Output: 4–20 mA + HART for standard volumetric flow
Example 3: Cooling Water
Application: Measure cooling water flow in a DN100 pipe. Temperature: 30°C. Flow range: 20–120 m³/h.
Selection:
Medium: Liquid → no compensation required (temperature is stable and well below boiling point)
Meter: Standard vortex flowmeter with piezoelectric sensor
Size: Calculate velocity. At 20 m³/h in DN100, velocity is approximately 0.7 m/s (above the 0.5 m/s minimum)
Output: 4–20 mA + pulse for totalisation
5. Common Mistakes to Avoid
| Mistake | Consequence | Prevention |
|---|---|---|
| Sizing by pipe diameter, not flow range | Meter operates below minimum velocity; signal loss at low flow | Calculate velocity at minimum and maximum flow; resize meter if necessary |
| No temperature/pressure compensation for steam or gas | Volumetric flow measured instead of mass flow; large errors with pressure/temperature changes | Use integrated multivariable meter or external compensation |
| Insufficient straight pipe runs | Swirl and turbulence cause inaccurate readings | Follow ISO 12764 and manufacturer requirements |
| Installing downstream of a partially open valve | Severe flow disturbance; measurement error | Install upstream of valves, or provide 20D+ upstream straight pipe |
| Using vortex for high-viscosity liquids | Weak vortex signal; poor accuracy | Verify viscosity is below 20 mPa·s; consider alternative technology |
| Ignoring Reynolds number at minimum flow | Non-linear operation below Re = 10,000 | Verify Re exceeds 10,000 at minimum flow |
| Inadequate vibration isolation | Signal noise; erratic readings | Avoid mounting near pumps, compressors, or vibrating equipment-26 |
| No drain/vent provisions for steam | Condensate accumulation; measurement errors | Install drip legs and steam traps upstream |
| Incorrect orientation for liquid service | Gas pockets in the meter; signal loss | Install with sensor on top of horizontal pipe |
| Using a standard meter for wet steam | Water droplets cause signal noise and errors | Verify steam quality; consider alternative technology for wet steam |
6. Applicable Standards
| Standard | Scope |
|---|---|
| ISO 12764:2017 | Measurement of fluid flow in closed conduits—flowrate measurement by means of vortex shedding flowmeters inserted in circular cross-section conduits running full. Describes the use of vortex shedding flowmeters for liquids, gases, and steam, including engineering equations for specifying performance- |
| ISO 5167 | Measurement of fluid flow by means of pressure differential devices—provides context for comparing vortex with DP flow measurement |
| BS ISO 12764:2017 | UK adoption of ISO 12764 |
7. Why Choose Anhui Tiankang for Vortex Flowmeters?
Anhui Tiankang (Group) Co., Ltd. has been manufacturing industrial instruments for nearly five decades. Our vortex flowmeters are designed for reliable performance across steam, gas, and liquid applications.
Vortex flowmeter product portfolio:
| Model | Type | Key Features |
|---|---|---|
| TK-VFM series | Standard vortex | Piezoelectric sensor, 4–20 mA + pulse, flange/wafer connections |
| TK-VFM-MV | Multivariable vortex | Integrated temperature and pressure sensors, compensated mass flow output |
| TK-VFM-HT | High-temperature vortex | Up to 400°C, ceramic sensor, high-temperature materials |
| TK-VFM-EX | Explosion-proof vortex | Ex d IIC T6 / Ex ia IIC T6, for hazardous areas |
Key specifications:
Sizes: DN15 to DN300 (standard); larger sizes available with insertion type
Accuracy: ±0.75% of reading (liquid); ±1.0% of reading (gas/steam)-
Turndown: Up to 20:1 for gas and steam; 10:1 for liquids
Temperature range: -40°C to +400°C (model-dependent)
Pressure rating: Up to PN100 (higher on request)
Body materials: 304 SS, 316L SS, Hastelloy C-276
Output: 4–20 mA, pulse, RS485/Modbus, HART
Protection: IP65/IP67; Ex d IIC T6, Ex ia IIC T6
Core advantages:
Complete certifications: CCC Ex, ATEX, IECEx, SIL
CNAS-accredited laboratory: Full performance testing including flow calibration
Engineering support: Sizing calculations, compensation design, installation guidance
Proven track record: Long-term supplier to CNPC, Sinopec, CNOOC, and international EPC projects
One-stop supply: From flowmeters to temperature/pressure transmitters to cables—one supplier, one interface
8. Conclusion
Selecting the right vortex flowmeter is a systematic process that starts with the medium, not the pipe size.
Key takeaways:
| Selection Step | Key Principle |
|---|---|
| Medium definition | Steam (saturated/superheated), gas, or liquid—determines compensation requirements |
| Flow range | Size by flow range, not pipe diameter; normal flow at 50–70% of range |
| Meter size | Calculate velocity at min and max flow; verify Reynolds number > 10,000 |
| Compensation | Steam: temperature or pressure (saturated) or both (superheated); Gas: both temperature and pressure; Liquid: generally not required |
| Materials | Match to process corrosiveness and temperature |
| Installation | 10D upstream, 5D downstream minimum; 20D+ after valves; avoid vibration sources |
| Verification | Confirm Reynolds number at minimum flow; verify velocity is within meter range |
The most important rule: A vortex flowmeter is a velocity device. It needs sufficient velocity to generate a measurable signal and sufficient Reynolds number to maintain linearity. If the application cannot provide these conditions at the minimum flow rate, the vortex flowmeter is the wrong choice—no amount of compensation or calibration will fix it.
Remember: The cost of proper selection is a few hours of engineering. The cost of poor selection is a meter that never works correctly, a process that cannot be controlled, and a replacement project that could have been avoided.
Contact Us
For vortex flowmeter selection advice, sizing calculations, or project quotations, please contact:
Yin Shuangjie
International Sales Manager
📧 Email: [email protected]
📱 WhatsApp / Zalo: +86 17856068126
🌐 Website: http://www.tiankang-global.com/
Anhui Tiankang – Your partner for reliable vortex flow measurement solutions.

