Why two batches of the same grade cost different money

The recipe is fixed. The equipment is the same. And yet the yield, the cycle time and the steam bill move batch to batch, and the reason usually arrives after the batch has shipped.

What we connect to in your plant

We read from your existing DCS and historian. Connection is passive — nothing is written back to the control system unless you explicitly ask for it and your controls team signs it off.

The signals we read, and what each one tells you

A tag on its own is noise. What matters is the question each one answers for the person standing at the machine.

Signal What it tells you
Internal and jacket temperature with ramp rate Exotherm control and whether this phase is tracking the profile that produced your best yields.
Agitator motor power draw Viscosity change, crystallisation onset, and impeller or seal trouble — long before anyone opens the manhole.
Dosing flow and totaliser per charge Addition-rate deviations, which is where a surprising share of yield variance originates.
Pressure, vacuum and reflux ratio Separation efficiency and the early shape of a column upset.
pH, conductivity and turbidity In-process quality indication hours before the lab confirms it.
ISA-88 phase timestamps Where cycle time actually goes — charging, reaction, workup, transfer, cleaning — instead of one number for the batch.
Steam, chilled water, nitrogen and power per batch True conversion cost per kilogram, by grade and by equipment train.
CIP cycle count and duration What each grade-to-grade transition really costs in cleaning time and solvent.
Effluent flow and load Environmental cost attributed back to the batch and grade that generated it.

Plant, quality and finance looking at the same batch

One record per batch that production, QA, EHS and costing all trust, because it comes from the instruments rather than from three separate spreadsheets.

Batch cycle time by phase

hours, against best-in-class

Golden-batch conformance

%, per phase

First-pass yield

%, by grade

Off-spec and rework rate

%, by grade

Steam per tonne

kg per tonne of product

Power per tonne

kWh per tonne

Solvent recovery

% recovered

Reactor and dryer occupancy

% of available hours

Changeover and CIP time

hours per transition

Cost per kilogram

currency, by grade

Effluent load per tonne

COD / BOD per tonne

Batch record closure time

hours from end of batch

AI trained on your process. Not a generic factory.

Models built on batch process behaviour — phases, recipes, campaigns and shared equipment — not on a generic time series.

Golden-batch fingerprint and live deviation

Builds the reference profile from your own best historical runs, then alerts phase by phase when the current batch drifts from it — with the correction still available to the operator rather than a post-mortem for the QA meeting.

Soft sensors for end-point prediction

Predicts assay, moisture or conversion from the live process signature, so the desk can decide whether to hold, extend or move on without waiting on the lab queue.

Specific-energy optimiser

Learns steam and power per tonne by grade, season and equipment train, then surfaces the setpoint combinations behind your cheapest good batches. Utilities usually hold the fastest payback in a specialty plant.

Campaign sequencer

Orders grades across shared reactors, dryers and centrifuges to cut cleaning cycles and changeover loss, while respecting the commitments you have already made to customers.

Your first thirty days

Read-only, one train, no DCS changes. The historian does most of the work in the first fortnight.

1

Tap the historian and one train

Read-only connection to the DCS or historian for a single reactor train. Tag mapping and cleanup happen here — this is usually the honest bottleneck, not the technology. 

 

2

Rebuild the last twelve months

Every historical batch of the chosen grade is reconstructed phase by phase and ranked. The golden profile emerges from your own data, not from a textbook.

3

Add lab and utilities

LIMS results and utility meters join the same timeline, so a batch can finally be costed end to end in currency per kilogram.

4

Run live deviation alerting

One grade goes live with phase-by-phase alerting. The desk sees a deviation while the correction is still possible.

What plants aim for in the first quarter

5–12%

batch cycle time reduction on the connected train

 

2–5 pts

first-pass yield improvement on the modelled grade

6–15%

reduction in steam and energy per tonne

30–50%

faster batch record closure

Target ranges for scoping a pilot. Replace with your own validated customer results before this page goes live.

Questions plant teams ask us first

Does anything get written back to our DCS?
No. The default is strictly read-only. Closed-loop control is possible later if you want it, but only as a separate, deliberate project run with your controls and safety teams.
Our historian has thousands of tags and inconsistent naming.
That is normal and it is part of week one. We map the tags that matter for the chosen train, build a consistent model around them, and leave you with documentation you did not have before.
Do we have to replace our LIMS or SAP?
No. Both stay exactly where they are. We read from them and join their data to the process timeline.
Is this a safety system?
No, and it should not be treated as one. It sits entirely outside your SIS and BMS. It is a data and decision layer, not a protection layer.
We run several plants and dozens of grades. Does that break the model?
It improves it. Models are built per equipment train and per grade family, which then lets you benchmark the same grade across sites and see which plant runs it best and why.