01 · Mixing & Shear

Compare agitator type and speed, lab vs. plant

Lab-scale mixing rarely replicates plant-scale shear forces. If the formulation is shear-sensitive, note it before scale-up.

Confirm vessel geometry and fill ratio at plant scale

Mixing efficiency changes with vessel shape and how full it's run — not just agitator specification.

02 · Heat Transfer

Calculate surface-area-to-volume ratio at bulk scale

This ratio drops sharply as batch size increases, directly changing heating and cooling rates.

Measure actual heat-up and cool-down time at plant scale

Don't assume the lab's heating curve — measure the plant vessel's real curve before finalizing process timing.

03 · Reaction & Dwell Time

Recalculate reaction/dwell time for bulk batch duration

Bulk batches take longer to process end-to-end — extended exposure time can shift outcomes even with an identical recipe.

Define an intermediate trial scale between lab and full bulk

An intermediate run against real plant parameters catches instability before it happens at full 1000kg volume.

04 · Water & Success Criteria

Compare water hardness and mineral content, lab vs. plant source

A different water source between lab and plant is a common, easily overlooked cause of scale-up drift.

Set a defined success criterion before the trial starts

Decide what "working" means in measurable terms before running the trial — not after looking at the result.

Read the Full Diagnosis

Already seeing instability at bulk scale?

See the detailed root-cause breakdown for scale-up instability, including how we structure the intermediate trial.

Read Scale-Up Instability Diagnosis →
Ready for the Next Step

Send us your plant parameters and we'll help structure the intermediate trial.

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