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SZSHIZHONGFlow Instruments

INDUSTRY SOLUTION

Power Generation flow measurement

Engineered DP measurement for main and auxiliary steam, feedwater, cooling water, combustion air and flue-gas duties in power and boiler systems.

ENGINEERING CONTEXT

The measurement challenge

Power-generation measurements combine high temperature and pressure, changing load, strict energy accounting and demanding mechanical integrity. Primary-element geometry must remain stable under velocity, thermal cycling and long service. Steam properties, pressure and temperature compensation, condensate management in impulse lines and the complete uncertainty budget can be as important as the element itself.

Common measurement duties

  • Main, reheated and auxiliary steam measurement
  • Boiler feedwater and condensate duties
  • Cooling-water and circulating-water systems
  • Combustion-air and flue-gas measurement
  • Boiler-performance and plant-utility monitoring

APPLICATION REVIEW

How we frame the engineering decision

For steam, the design establishes whether the operating envelope remains single-phase and whether mass or energy flow is required. A validated property formulation such as IAPWS-IF97 should use measured absolute pressure and temperature where density variation is material. Pressure and temperature can confirm superheat or proximity to saturation, but they do not determine dryness fraction on the saturation line. Wet-steam service lies outside the ordinary single-phase ISO 5167 coefficient basis unless a validated method specifically covers it.

Flow nozzles are commonly evaluated for clean, high-velocity or high-temperature service because their rounded inlet does not depend on the sharp upstream edge of an orifice plate. ISO 5167-3 defines separate requirements for ISA 1932, long-radius and Venturi-nozzle geometries. Classical Venturi tubes can reduce permanent pressure loss in continuously operated water or utility lines when their ISO 5167-4 construction and installation limits are satisfied. Large ducts may justify an averaging differential-pressure probe with a project-specific performance basis.

Impulse systems for steam require matched pressure legs, correct elevation, condensate management and a commissioning procedure that protects personnel and equipment. Materials, welds, pressure rating, thermal expansion, creep, vibration and inspection follow the plant piping code and specification. The sizing report should show differential pressure, permanent loss and combined uncertainty at minimum, normal and maximum load rather than one headline accuracy figure.

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

Why are flow nozzles frequently considered for main-steam service?

Their rounded inlet is mechanically robust for clean, high-velocity service and ISO 5167-3 provides defined geometries and coefficient methods within stated limits. Final suitability still depends on pressure, temperature, materials, Reynolds number, straight run and project requirements.

Can pressure and temperature compensation correct wet steam?

Not by itself. A pressure-temperature pair cannot determine dryness fraction on the saturation line. If wet-steam mass or energy flow matters, the project needs an approved steam-quality measurement or a validated wet-steam method with a stated operating range and uncertainty.

Ready to discuss your application?

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

ISO 9001TS Licensed30+ PatentsSince 1989
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