Biodiesel · chemical process model

How to model a biodiesel plant in Acatian

Connect feed quality and reaction chemistry to separation, methanol recovery, product specification, utilities and plant economics.
How to model a biodiesel plant in Acatian in the Acatian flowsheet workspace
One flowsheet connects assumptions, balances, equipment, time, economics and evidence.
Oil receiptPretreatmentReactionPhase splitPurificationMethanol recoveryProducts

Engineering brief

Model the complete decision, not an isolated unit operation.

Biodiesel performance depends strongly on oil quality. Acatian can distinguish triglycerides, free fatty acids, water, catalyst, alcohol, esters, glycerol and impurities so pretreatment and downstream separation remain visible.

The model can compare homogeneous or alternative catalytic routes without collapsing product, glycerol, methanol recovery, wash water and waste into a single conversion factor.

01 · Model basis

What the Acatian model needs to resolve

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

Inputs

Data

Oil composition, FFA, moisture and delivered cost

Evidence

Alcohol ratio, catalyst, conversion and residence time

Plant

Settling, centrifugation, washing or dry-purification data

Basis

Methanol recovery, glycerol quality and fuel specification

Mechanisms

Balance

Reaction stoichiometry and conversion

Model

Liquid-liquid phase and component allocation

System

Alcohol recycle and purge convergence

Time

Heating, separation and utility balances

Constraints

Limit

FFA and water limits

Risk

Soap/emulsion formation and separation

Capacity

Methanol recovery and safety

Gate

Fuel and glycerol product specifications

Outputs

Result

Biodiesel yield, purity and feed demand

Decision

Alcohol, catalyst, wash and energy use

Plant

Glycerol and waste streams

Value

Throughput, cost and feedstock sensitivity

02 · Acatian workflow

Build it in six controlled steps

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

    Define feed assay and product specifications.

  2. 02

    Add pretreatment for FFA and water.

  3. 03

    Close reaction stoichiometry by component.

  4. 04

    Model phase split and purification.

  5. 05

    Converge methanol recovery and recycle.

  6. 06

    Evaluate capacity, TEA and uncertainty.

03 · Decisions

Questions the model should answer

Which feed quality needs pretreatment?

Which purification route fits the water boundary?

How valuable is methanol recovery?

What feed-price range preserves margin?

04 · Evidence boundary

Validate before the result carries weight

Validation

Reconcile conversion, ester specification, phase yields, residual methanol, catalyst loss, energy and elapsed time against representative feed lots.

Limitations

The process model does not replace flammability, pressure, hazardous-area, materials, emissions or fuel-certification engineering.

Frequently asked questions

Practical modelling questions

Can waste oils be modelled?

Yes. FFA, water and impurities should be measured and routed through explicit pretreatment and uncertainty cases.

Can methanol recycle be closed?

Yes. Recovery, purity, purge and makeup can be iterated to a declared convergence tolerance.

Can coproduct glycerol be valued?

Yes, but its composition, purification need, sale assumption and uncertainty should be explicit.

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.