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

QEM & OPS logo

Steam & Energy

Energy Efficiency

Most amine units use more steam than they need. The twin shows how much.

Reboiler steam is the largest running cost of an amine unit. The digital twin measures it honestly, names the faults that push it up, and searches the settings you approve for the lowest steam that still treats the gas to specification.

11.1%Median steam cut from set-points alone
2×The saving at the plant’s best recorded point
7.8–14.7%95% confidence range of the cut
0Limits allowed to worsen: gas quality, amine loss, pump power

Case studyIndustrial MDEA gas treating unit, 13 days of one-minute data. Savings are steady-state potential from the model, awaiting a plant trial.

Measure it, explain it, then reduce it.

01

Measure the honest number

Steam per tonne of feed moves every time the feed changes. Steam per tonne of acid gas removed follows the work the unit is actually doing. The platform trends both, and ranks ten signals against the honest one, so the strongest bar shows where to look first.

02

Name what is wasting it

Exchanger fouling, reboiler scaling, over-stripping and poor steam supply all raise steam quietly, for months. Each is a named fault with its evidence, and the excess energy it causes carries a cost per hour.

03

The plant was over-stripping

In the case study the unit was stripping harder than the gas needed. Cutting steam and circulation together held the lean loading and the treated gas on specification. The twin found this move without being told to look for it.

04

Search, then check with the diagnosis

The Optimise tool searches lean circulation, reboiler steam and antifoam inside the ranges you approve. The winning point is then run through the full fault diagnosis. Without that check, 43% of proposals would have raised a fault, a warning or an extra amine loss.

Where the evidence stops

  • The 11.1% is steady-state potential calculated by the model, not a measured saving. It holds within the range of steam rates the plant has actually used. Below that range the model points to up to 20%, but that needs a staged plant trial to confirm. The platform advises; it does not write to your control system.

The steam number is the easiest one to check.

See steam per tonne of acid gas, and the saving the Optimise tool finds, running on real plant data.

Request a demo