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Application

Valve and Airlock Selection for Chemical Powder Lines

Answer in brief

In chemical plants the valve is rarely chosen for throughput; it is chosen for what the powder does to it and for what it must not let past.

Corrosive and hygroscopic solids attack seats and clearances, and most lines cross a pressure boundary somewhere between the silo and the reactor.

  • Fix the material of construction before the valve type.
  • State the acceptable gas leakage, because it sets the clearance class.
  • Plan the changeover procedure before the line is built.

Reviewed October 21, 2026 · Updated October 21, 2026

The problem

Chemical powder lines carry products that are aggressive, hygroscopic or both, and they usually run several grades through the same equipment.

A valve chosen on price corrodes at the seat, opens its clearance and leaks conveying gas into a vessel that was supposed to stay inert.

Desired outcome

A valve that holds its sealing function for a defined service life, tolerates the cleaning regime between products and leaks no more gas than the process design allows.

Process approach

Start with the pressure boundary. Where a conveying line is pressurised, the valve is a gas barrier before it is a solids handler, and the permitted leakage sets the clearance and the seal design.

Rotary valves feed continuously into pressure lines, and their leakage is a design value that grows as clearances open with wear.

Slide gates isolate vessels and are specified for a tight shut-off under a material column rather than for metering.

Diverter valves route one stream between reactors, dryers or packing lines, and here the question is whether the junction can be cleaned between products.

  • Stainless grades, special alloys or polymer linings chosen from the actual product list, including cleaning agents.
  • Shaft seals selected for the dust and for any purge gas the process requires.
  • Quick-clean designs where the plant changes product more than a few times per week.

Selection factors

  • Corrosion behavior of every product and cleaning medium against the contact materials.
  • Permitted gas leakage across the valve, and how it will be measured in service.
  • Abrasiveness of crystalline solids, which decides clearance life.
  • Changeover procedure and the access needed to carry it out.
  • Area classification, where the dust or a solvent residue makes it relevant.

Common failure modes

  • Seat corrosion opening the clearance and raising gas leakage
  • Product build-up in the valve pocket after a changeover
  • Shaft seal failure releasing dust into the room
  • Valve used as a feeder, giving a rate that drifts with head

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