Now live: a hybrid process digital twin for amine gas sweetening — it names the fault and the root cause, not just the alarm. Explore the platform →

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Chemical Plants

If the process removes acid gas, the model already knows the shape of it.

Ammonia, syngas, hydrogen and ethylene oxide plants all run a CO₂ removal loop on amine or hot potassium carbonate. The solvent changes. The structure and the failure modes do not.

Applicable — needs calibrationNeeds datasheets and a calibration pass.

Aerial view of process piping and equipment

The unit we model

Absorber, flash, lean/rich exchange, regenerator and reboiler — the circulating-solvent loop that every acid gas removal unit is built from.

What it finds

Foaming, fouling, corrosion, filter bypass and solvent degradation: the failure modes shared by any unit that circulates a solvent through a hot regenerator.

What it takes to start

Equipment datasheets, a tag list, and a calibration pass against your own history. This is engineering work, not a configuration screen — and we would rather say so now.

Scope on your site

What is inside the model, and what is not.

  • Ammonia and syngas CO₂ removal
  • Hydrogen plant acid gas removal
  • Ethylene oxide CO₂ removal
  • Tail gas treating

Ten minutes in the platform beats an hour of slides.

It runs on a real amine train with thirteen days of one-minute history behind it — live diagnosis, root causes and cost per hour. Nothing on this page is a mock-up.

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