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SZSHIZHONGFlow Instruments

INDUSTRY SOLUTION

Chemical & Petrochemical flow measurement

Application-specific DP primary elements for corrosive, viscous, crystallizing, solids-bearing and variable process streams, with materials and maintainability considered from the start.

ENGINEERING CONTEXT

The measurement challenge

Chemical processes often combine difficult fluid behavior with restricted piping layouts and demanding materials. A high-viscosity liquid can move across a wide Reynolds-number range; deposits can change an effective flow area or block pressure taps; corrosion and erosion can alter the calibrated geometry. Reliable selection therefore joins process chemistry, phase behavior, mechanical design, measurement uncertainty and maintenance access rather than treating them as separate purchasing decisions.

Common measurement duties

  • Corrosive and hazardous liquid measurement
  • Viscous, crystallizing and solids-bearing service
  • Reactor-feed and process-unit flow control
  • Plant steam, gas, water and utility balancing
  • Retrofit studies for restricted piping layouts

APPLICATION REVIEW

How we frame the engineering decision

Selection begins with composition, concentration, solids content, viscosity across the operating temperature range and any tendency to polymerize, crystallize, flash or release gas. These properties determine the usable Reynolds-number range, pressure-tap arrangement and whether a standardized coefficient applies. Wedge meters can be considered for viscous or solids-bearing duties when the ISO 5167-6 limits or a representative calibration cover the actual design. Clean, single-phase utilities may be better served by a standardized orifice, nozzle or Venturi.

Wetted materials are selected from the project corrosion study and piping specification, not from a generic stainless-steel rule. Base material, cladding or lining, gaskets, fasteners, pressure taps, impulse tubing and any diaphragm seal must be compatible with the process and cleaning method. Design pressure and temperature, corrosion allowance, fabrication, heat treatment and inspection requirements remain governed by the applicable mechanical code and customer specification.

Maintainability is part of measurement performance. Flush ports, remote seals, purging, heat tracing or enlarged taps may be needed, but each modification must be included in the documented coefficient or calibration basis. The installation review also identifies control valves, elbows, reducers and branches that can distort the velocity profile. Where straight pipe is limited, use a documented short-run arrangement or calibration rather than assuming that a compact device is automatically insensitive to disturbances.

RECOMMENDED FAMILIES

A practical starting point

These product families form an initial shortlist. Final geometry, coefficient basis, materials, transmitter arrangement and installation requirements are confirmed from the complete process duty.

Recommendations remain preliminary until process conditions and project requirements are reviewed.

TECHNICAL RESOURCES

Continue the application review

FREQUENTLY ASKED

Questions at the RFQ stage

Which DP meter is suitable for a viscous or crystallizing liquid?

A wedge meter is often evaluated because its open flow path can suit viscous and deposit-prone service, but suitability depends on viscosity, Reynolds number, solids, tap design, temperature control and the applicable standard or calibration range. The result cannot be selected from viscosity alone.

Can purging or diaphragm seals be added without affecting accuracy?

They can be used when properly engineered, but they change the pressure-transmission system and can add zero shift, response delay, temperature effects or purge-flow bias. The final arrangement must be included in commissioning and uncertainty review.

Ready to discuss your application?

Send your process data for an engineering review and a project-specific next step.

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