Circulation is a steam bill.Stop treating the worst case.

INSUS recommends the lowest solvent circulation required for the gas you are actually treating, while keeping treated-gas quality and rich loading within defined limits. Process engineers approve every change.

  • 01

    Reboiler steam and circulation are linked.

  • 02

    Treated-gas specification stays protected.

  • 03

    Rich loading remains a hard integrity constraint.

The problem

The optimum is bounded.Operation often isn't.

An amine unit has a real operating window. Circulate too little and treated gas can go off-spec or rich loading can move toward corrosion risk. Circulate too much and the unit pays for unnecessary regeneration steam, pumping power and solvent handling. The feed changes continuously, but the circulation rate is often held around a standing margin sized for the worst case.

Amine unit optimisation window showing treated gas specification and rich loading constraints
01
02
03
  • 01Too little circulation
  • 02Treated gas specification
  • 03Rich loading limit

The shift

From standing circulationto feed-matched operation.

The treated-gas specification and integrity limits stay defined. The feed does not. What changes is matching the recommendation to the gas actually entering the unit instead of continuously carrying worst-case circulation margin.

Today

Circulation built around the worst case

  • Circulation held at a standing rate sized for difficult feed conditions.
  • Rich loading checked periodically through solvent analysis.
  • Reboiler duty follows circulation without continuously questioning the margin.

With INSUS

Circulation matched to current feed

  • Circulation recommended against current feed composition and flow.
  • Rich loading estimated between laboratory analyses with margin visible.
  • Reboiler duty minimised subject to treated-gas and loading constraints.

How it works

From feed gasto a safer circulation setpoint.

This fits OptiStudio as treating decision support above the existing amine unit control strategy. Access is read-only. Rich loading limits are mechanical-integrity boundaries, not variables to trade away for energy savings.

  1. Connect

    Bring the amine unit data together

    Connect feed gas flow, composition and conditions; absorber pressures and temperatures; lean and rich solvent flow and temperature; solvent loading and concentration; regenerator conditions; reboiler duty or steam flow; treated-gas analyser readings; and solvent-management records.

  2. Understand

    Learn how this unit responds

    Model the relationship between circulation, solvent condition, feed composition and operating conditions to understand how treated gas quality and rich loading actually respond on the specific amine train.

  3. Predict

    Predict quality and loading

    Estimate treated-gas acid-gas content and rich loading at candidate circulation rates, including uncertainty. Where solvent-condition data supports it, indicators associated with foaming or solvent degradation can also be flagged.

  4. Advise

    Find the minimum safe circulation

    Advise the lowest circulation and associated regeneration duty that meets the treated-gas specification while keeping rich loading below its corrosion-related limit with appropriate operating margin. Process engineers decide.

  5. Verify

    Validate against the real unit

    Compare predictions with treated-gas analyser readings and routine rich-loading analyses. Constraint excursions are treated as model failures rather than an acceptable cost of optimisation.

OptiStudio advisory layer connected to an existing amine gas treating unit

Getting started

Start with one amine trainand the feed changes you already ran.

For acid-gas removal units where circulation is held for the worst case. Delivered through OptiStudio as treating decision support. Expert Services can help with data assessment and validation. Advisory and read-only. Does not replace the DCS.

  • What we need. Feed composition, flow, pressure and temperature; absorber and regenerator conditions; solvent circulation; treated-gas analyser readings; reboiler steam or duty; and routine solvent analyses including rich loading and heat stable salts. No new sensors where those already exist.
  • What you see first. A historical back-test of the rich-loading soft sensor against laboratory analyses on one amine train, and circulation recommendations checked across feed-composition changes before any live advice.
  • Where the limits are. Advisory and read-only. Process engineers retain control over every operating change. Rich loading remains a hard integrity constraint. Performance must be validated against the customer's own train. No plant-specific savings claim is quoted in advance.
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Questions process engineers ask us

Amine units often carry circulation margin for sour-gas variability, which raises reboiler steam and pumping power. This use case advises the lowest circulation that still meets treated-gas quality and rich-loading limits for process engineer review.

Feed composition, flow, pressure and temperature; absorber and regenerator conditions; solvent circulation; treated-gas analyser readings; reboiler steam or duty; and routine solvent analyses including rich loading and heat stable salts. No new sensors where those already exist.

No. It is an advisory optimisation layer. Existing DCS control remains responsible for operating the unit. The pilot is read-only; process engineers retain control over every operating change.

No by design. The rich-loading limit is a hard mechanical-integrity constraint. The advice is not designed to trade corrosion margin for energy savings, and any constraint excursion is treated as a model or operating issue requiring investigation.

Through OptiStudio as treating decision support. Expert Services can support data assessment, integration and validation with your process team.

Yes, where the required process and solvent data is available. LNG pretreatment can involve particularly tight treated-gas specifications because acid-gas removal is required before cryogenic processing.

Where rich-loading analysis is infrequent, the soft sensor becomes more valuable but needs more careful validation. Quality and integrity constraints remain hard limits on every recommendation. No plant-specific savings claim is quoted before seeing your train.

Processing · Acid gas removal

How much circulation is actually necessary?

A back-test on your own amine train will show where circulation is providing useful absorption margin and where it is simply carrying insurance, with treated-gas specification and rich-loading integrity visible in every recommendation.