Extreme close-up of a flanged vortex flow meter mounted on a large steam header pipe, gauge face showing live pressure reading, copper-toned instrument body catching ambient amber work-site light, real industrial pipe insulation and condensation visible, overcast daylight, desaturated steel background
Extreme close-up of a flanged vortex flow meter mounted on a large steam header pipe, gauge face showing live pressure reading, copper-toned instrument body catching ambient amber work-site light, real industrial pipe insulation and condensation visible, overcast daylight, desaturated steel background
— Proven Deployments

Real conditions. Exact meter. No overspec.

Steam headers, viscous liquids, high-pressure gas—each installation documented with the operating constraints that drove the selection.

Close-up of a clamp-on ultrasonic flow meter installed on a heavily insulated high-temperature steam header in a boiler room, condensation on adjacent fittings, overcast north-facing work-site light, steel and lagging in frame, no people, desaturated palette
Close-up of a clamp-on ultrasonic flow meter installed on a heavily insulated high-temperature steam header in a boiler room, condensation on adjacent fittings, overcast north-facing work-site light, steel and lagging in frame, no people, desaturated palette
Hands adjusting the sensor head of a Coriolis flow meter on a crude oil transfer line, amber instrument indicator light glowing against desaturated steel pipe, oily residue on fittings, overcast work-site daylight, industrial pipe rack in background, tight framing
Hands adjusting the sensor head of a Coriolis flow meter on a crude oil transfer line, amber instrument indicator light glowing against desaturated steel pipe, oily residue on fittings, overcast work-site daylight, industrial pipe rack in background, tight framing
Wide shot of a compressed gas metering skid in an outdoor compressor station, multiple flanged differential-pressure transmitters and impulse lines visible, overcast daylight, galvanized steel structure, gauge faces showing high-pressure readings, no people, muted industrial palette
Wide shot of a compressed gas metering skid in an outdoor compressor station, multiple flanged differential-pressure transmitters and impulse lines visible, overcast daylight, galvanized steel structure, gauge faces showing high-pressure readings, no people, muted industrial palette
/ Three Application Cases

Different fluids, different answers

High-Temperature Steam

Confined header, no process interruption

Saturated steam at 185°C in a header with less than 30 cm clearance. Insertion meters were ruled out—line pressure couldn't be broken. A clamp-on ultrasonic unit resolved it without shutdown.

Technology selected: non-invasive ultrasonic. Constraint that ruled out alternatives: zero-downtime requirement and header insulation depth.

Viscous Crude Liquid

Variable rates, high-viscosity crude

Crude oil at 8–200 cP viscosity across a 10:1 turndown range. Electromagnetic meters dropped off the list—non-conductive fluid. A Coriolis unit matched the full range without recalibration at shift changes.

Technology selected: Coriolis mass meter. Constraint that ruled out alternatives: wide viscosity swing and non-conductivity of the process fluid.

Compressed Gas, Extreme Pressure

300 bar line, custody-transfer accuracy

Natural gas at 300 bar in a custody-transfer application. Vortex meters weren't rated for the pressure class. A differential-pressure transmitter with a conditioning orifice plate met both the pressure rating and the ±0.5% accuracy specification.

Technology selected: DP with conditioning plate. Constraint that ruled out alternatives: 300 bar pressure class and custody-transfer accuracy threshold.

+ Operating Envelope

What we've measured—and at what limits

Liquids
Steam
Gases

Conductive, non-conductive, viscous

Saturated and superheated, up to 400°C

Compressed, custody-transfer, corrosive

Water, crude, chemicals, slurries. Viscosity range up to 500 cP. Electromagnetic, Coriolis, and ultrasonic technologies selected by fluid conductivity and flow profile.

Boiler headers, distribution mains, and process steam. Non-invasive ultrasonic or vortex selected based on header access, pressure class, and whether the line can be tapped.

Natural gas, nitrogen, chlorine, and mixed process gases. Pressure ratings to 400 bar. DP, thermal mass, and ultrasonic selected against accuracy spec and gas composition.

We've solved this before—probably harder

Give us your fluid, pressure, temperature, and installation constraints. We'll return a specific meter recommendation, not a product list.