What the season costs you, and when you find out

Most of these numbers exist somewhere in the mill today. The problem is that they arrive weeks late, from four different departments, after the cane they refer to has already been crushed.

What we connect to in your plant

A sugar mill is really four plants sharing a season — cane handling, milling, boiling house and cogeneration. We connect them as one system, because that is how the losses move between them.

The signals we read, and what each one tells you

During the season, the only signals worth having are the ones that change a decision before the next shift starts.

Signal What it tells you
Cane crushed per hour against rated capacity Crush rate loss as it happens, rather than as a weekly average that hides the bad nights.
Stoppage start and stop with section tags Downtime split cleanly across mills, boiler, cogen, electrical and cane shortage, without anyone maintaining a register.
Mill hydraulic pressure, roller torque and imbibition flow The settings behind extraction, captured alongside the shift that chose them.
Preparation index and fibrizer motor current Cane preparation quality, which sets the ceiling on everything the tandem can achieve downstream.
Bagasse moisture and pol in bagasse Milling loss attributed to a shift and a set of settings instead of to the season as a whole.
Brix, pol and purity across juice, syrup, massecuite and molasses Where sucrose is actually being lost between the mill and the bag.
Evaporator vapour pressure, pan cycle time, centrifugal cycle and load Boiling house throughput and the bottleneck that is really limiting it.
Boiler steam flow, pressure, temperature and bagasse feed Steam percent cane, live, which is the number that converts into exportable power.
Turbo-generator export and auxiliary consumption Net exportable power by shift, and where in-house load is eating it.
Weighbridge tickets and harvest timestamps Cane staleness before crushing, and the sucrose lost before the first mill ever sees it.

Season performance, updated by the shift

The numbers your management committee reviews weekly, available while there is still season left to act in.

Crushing rate vs capacity

TCD and %

Capacity utilisation

% of available hours

Downtime hours by cause

hours, ranked by section

Sucrose recovery

%

Reduced boiling house recovery

%

Pol % bagasse

%, by shift

Total losses

%, split by stream

Steam % cane

%

Power exported

MWh per day

Auxiliary power

% of generation

Imbibition %

% on cane

Sugar quality

ICUMSA and grain size

Cane staleness

hours harvest to crush

Season progress vs plan

tonnes crushed

AI trained on your process. Not a generic factory.

Models that understand a crushing season — where capacity is fixed, the clock does not stop, and every loss is measured against a window that closes.

Stoppage classifier and choke prediction

Learns the current and pressure patterns that precede cane carrier chokes, mill jams and centrifugal trips, and tags every stoppage to a section and a cause without anyone maintaining a register.

Recovery loss attribution

Ties pol in bagasse and in final molasses back to mill settings, imbibition rate, preparation index and shift, so the loss has an owner and a specific correction rather than a season-end discussion.

Steam percent cane optimiser

Finds the boiler and process setpoint combinations that produced the lowest steam per tonne of cane, turning saved bagasse into exportable power during the season it was saved.

Crush plan against cane arrival

Forecasts arrivals against yard stock and current crush rate to cut staleness and avoid both mill starvation and yard overflow, which are the two ways a good crushing day gets wasted.

Your first thirty days

Connection is read-only and done one section at a time. Nothing about it requires you to stop crushing.

1

Connect the tandem and weighbridge

Milling tandem instrumentation and weighbridge data, read-only. Crush rate against capacity becomes visible by the hour rather than by the week.

 

2

Automate the stoppage log

Stoppages get captured and classified from the machines, and last season's downtime is rebuilt so this season has something honest to be measured against.

3

Add the boiling house and lab

Brix, pol and purity join the process timeline, and the loss balance across bagasse, filter cake and molasses becomes a live picture.

4

Bring in cogeneration

Boilers and turbo-generators come on, giving steam percent cane and net export by shift — usually the first number that pays for the project.

What plants aim for in the first quarter

1–3%

increase in capacity utilisation from recovered crushing hours

 

0.1–0.3 pts

improvement in sucrose recovery

2–6%

reduction in steam percent cane, converted to export

same shift

visibility of losses, instead of post-season analysis

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

Questions plant teams ask us first

The season is already running. Can we start now?
Yes. Connection is read-only and done section by section, typically during routine cleaning stops. No crushing time is given up to install it, and the sooner it starts the more of this season it can measure.
Wouldn't the off-season be the better time?
The off-season is the best time to instrument, and the worst time to learn anything, because the plant is not running. Most mills instrument in the off-season and rebuild the previous season's history at the same time so the models are ready on day one of crushing.
Our laboratory is entirely manual.
That stays workable. Lab results are entered on a tablet with validation at the point of measurement, and land on the same timeline as the process data. Over time, soft sensors reduce how much the decision has to wait for the sample.
Our cogeneration relays are on IEC 61850.
Supported. Turbo-generator, relay and energy meter data come into the same timeline as crushing, which is what makes steam percent cane and net export a live number instead of a monthly calculation.
We have an integrated distillery. Can it be included?
Yes. Molasses balance, distillery utilities and steam sharing between the sugar plant and the distillery can be brought into the same picture, which is usually where the argument about steam allocation gets settled.