Biogas · anaerobic digestion

How to model anaerobic digestion and a biogas plant

Turn substrate assays and loading policy into gas production, digester capacity, heat demand, digestate flow and project economics.
How to model anaerobic digestion and a biogas plant in the Acatian flowsheet workspace
One flowsheet connects assumptions, balances, equipment, time, economics and evidence.
Feed receptionBlendingDigestionGas storageCHP / upgradingDigestateExport

Engineering brief

Model the complete decision, not an isolated unit operation.

A biogas model must preserve feed variability and time. Acatian can connect volatile-solids loading, degradation, inhibition and hydraulic residence time to daily gas production and downstream capacity.

The complete plant boundary includes reception, storage, pasteurization where applicable, mixing, heating, gas handling, flare, CHP or biomethane upgrading, digestate treatment and parasitic loads.

01 · Model basis

What the Acatian model needs to resolve

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

Inputs

Data

Wet mass, total and volatile solids, COD and biodegradability

Evidence

Feed cadence, blend limits and storage inventory

Plant

Methane potential, degradation rates and inhibition evidence

Basis

Digester volume, temperature, mixing, gas and digestate equipment

Mechanisms

Balance

Substrate and COD/VS balances

Model

First-order or calibrated digestion kinetics

System

Gas composition, storage and conversion

Time

Inventory, heat and electrical balances

Constraints

Limit

Organic loading and hydraulic residence time

Risk

Ammonia, VFA, pH and trace-element limits

Capacity

Gas storage, flare and upgrader throughput

Gate

Feed seasonality and digestate outlets

Outputs

Result

Methane production and uncertainty

Decision

Required active digester volume

Plant

Net electricity, heat or biomethane output

Value

Digestate, emissions, cost and availability scenarios

02 · Acatian workflow

Build it in six controlled steps

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

    Create a traceable assay for every feedstock.

  2. 02

    Define blending, storage and feeding events.

  3. 03

    Calibrate conversion and gas composition.

  4. 04

    Size digester, gas and digestate operations.

  5. 05

    Overlay availability and seasonal inventory.

  6. 06

    Compare energy, economic and environmental cases.

03 · Decisions

Questions the model should answer

Which feed blend is stable and valuable?

Does gas storage decouple production and demand?

CHP or upgrading: which fits the local boundary?

How much feed variability can the design absorb?

04 · Evidence boundary

Validate before the result carries weight

Validation

Validate gas yield, methane fraction, residual solids, heat demand and dynamic response against independent operating periods, not only BMP tests.

Limitations

The model does not replace biological safety review, gas-area classification, pressure protection, digestate regulation or emissions permits.

Frequently asked questions

Practical modelling questions

Can multiple wastes be blended?

Yes. Each feed can carry its own composition, availability, price and uncertainty before blending constraints are applied.

Can Acatian model biomethane upgrading?

Yes. Recovery, methane slip, electricity, consumables and product specification can be represented.

Can seasonal feed supply be scheduled?

Yes. Inventory and feed events can be evaluated against digester and gas-handling capacity.

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.