Industrial enzymes · production model

How to model industrial enzyme production in Acatian

Translate activity, titer and recovery into formulated product, equipment demand, utility load and COGS.
How to model industrial enzyme production in Acatian in the Acatian flowsheet workspace
One flowsheet connects assumptions, balances, equipment, time, economics and evidence.
MediaSeedFermentationClarificationConcentrationFormulationPack

Engineering brief

Model the complete decision, not an isolated unit operation.

Enzyme manufacturing is governed by activity and formulation specification, not mass alone. Acatian can retain enzyme activity, impurities, solids, water and formulation components through the flowsheet while also closing the physical mass balance.

The model makes upstream and downstream trade-offs visible: a titer improvement may reduce fermentation capacity but alter viscosity, clarification or concentration duty.

01 · Model basis

What the Acatian model needs to resolve

Inputs, mechanisms, limits and outputs remain reviewable on one declared basis.

Inputs

Data

Activity assay, titer, productivity and stability

Evidence

Media and fermentation recipe

Plant

Cell and solids properties, clarification performance

Basis

UF concentration, stabilizer, drying and formulation specification

Mechanisms

Balance

Fermentation state and activity balances

Model

Solids removal and yield accounting

System

Membrane concentration and diafiltration

Time

Activity loss, blending and packaging basis

Constraints

Limit

Broth rheology and oxygen transfer

Risk

Clarifier or filter solids loading

Capacity

Membrane flux and product passage

Gate

Thermal and storage stability

Outputs

Result

Activity units per batch and per year

Decision

Step yield and activity loss

Plant

Equipment, water and energy demand

Value

COGS per activity unit and sensitivity

02 · Acatian workflow

Build it in six controlled steps

Each step creates a reviewable object, not a hidden spreadsheet assumption.
  1. 01

    Define the saleable activity specification.

  2. 02

    Build component and activity ledgers.

  3. 03

    Calibrate fermentation and stability.

  4. 04

    Model solids removal and concentration.

  5. 05

    Add formulation, drying and packaging.

  6. 06

    Schedule campaigns and compare cost scenarios.

03 · Decisions

Questions the model should answer

Is titer or activity recovery more valuable?

Liquid concentrate or dried formulation?

Which step causes the largest activity loss?

How does broth variability affect plant capacity?

04 · Evidence boundary

Validate before the result carries weight

Validation

Check activity as well as mass across independent fermentation, recovery and stability studies. Confirm flux, fouling and drying assumptions at representative scale.

Limitations

The model does not replace product-specific safety, regulatory, allergen, containment or quality validation.

Frequently asked questions

Practical modelling questions

Can activity units be tracked separately from mass?

Yes. A model can track both a physical component balance and product activity with step-specific decay or loss.

Can secreted and intracellular enzymes be compared?

Yes. Cell disruption, solids load and recovery architecture remain explicit.

Can liquid and powder products be compared?

Yes. Formulation, evaporation or drying, stability, packaging and energy can share one annual basis.

Related engineering guides

Continue through the connected model.

Bring one real process question

Build a model your technical team can inspect, challenge and improve.

Start with customer-owned data, explicit acceptance criteria and a clearly bounded engineering decision.