S02·T

Techno-economic analysis that survives an investment committee.

A techno-economic analysis (TEA) is only as good as the balance underneath it. We build mass and energy balances from first principles, cost equipment from quotes and benchmarks, state the accuracy class, and show which assumptions actually move the return — so the number can be defended, not just presented.

Scope
Mass & energy balance · CAPEX · OPEX · returns
Accuracy
AACE Class 5 → Class 3, stated per estimate
Model
Scenario, sensitivity and break-even analysis
Pairs with
LCA, GHG Scopes 1–3, EU Taxonomy / CSRD data

What you get

First-principles mass & energy balance

Stream-by-stream balance calibrated against pilot or operating data where it exists, with yields and utility demand traceable to physics rather than a vendor slide.

CAPEX base with explicit contingency

Equipment list priced from budgetary quotes and benchmarks, installation factors named, indirects and contingency separated, and an accuracy class attached to the total.

OPEX and cost-of-production model

Feedstock, energy, consumables, labour and maintenance built into a unit cost of production at realistic utilisation and ramp-up, not nameplate.

Returns, sensitivity and break-even

NPV, IRR and payback with tornado sensitivity on feedstock price, product price, yield, energy cost and utilisation — plus the break-even conditions the case depends on.

TEA + LCA in one dataset

The same balance feeds the life-cycle assessment, so carbon and cost results are consistent and environmental claims carry numbers.

How it runs

  1. 01

    Fix the question and the gate

    Agree what decision the TEA feeds — screening, FID, permit or investor diligence — and the accuracy class that decision requires.

  2. 02

    Build the balance

    Process configuration and block flow, then a mass and energy balance per stream with named assumptions and data sources.

  3. 03

    Cost it honestly

    Equipment sizing to quotes, installation and indirect factors, and an OPEX model at the operating point the plant will actually run at.

  4. 04

    Stress the case

    Scenario and sensitivity runs, ramp-up curves, and identification of the two or three variables that decide the outcome.

  5. 05

    Hand over a defensible model

    Open model, assumption register, risk list and a written recommendation — including a recommendation not to invest when that is the honest answer.

  • TEA delivered from FEL-1 concept screening through FEL-3 definition, with the accuracy class stated on every estimate.
  • 30+ feasibility, pre-engineering and consulting assignments across biorefineries, biofractionation and extraction plants.
  • Cost bases written by the team that also executes delivery, so estimates reflect real installation and commissioning effort.
  • Consistent TEA and LCA outputs supporting EU Taxonomy and CSRD reporting and GHG Scopes 1–3.

From our own project record

Process flow diagram extract used as the basis for a techno-economic analysis
Process flow · Balance basisTEA input
3D plant cutaway model used to check layout and installation scope during cost estimation
Plant cutaway · Installation scopeCAPEX check

Client, site and product identifiers removed — most of our work is under NDA.

Most weak investment cases fail on the same two things: a balance that was never closed and a CAPEX with hidden contingency. A TEA done properly exposes both before the money moves.