Independent model study · circular materials

Close every metal before comparing battery-recycling routes

Trade Ni, Co, Li and Cu recovery against reagent demand, impurity rejection, water recycle, energy and residue as feed chemistry changes.
Close every metal before comparing battery-recycling routes in the Acatian flowsheet workspace
One flowsheet connects assumptions, balances, equipment, time, economics and evidence.
ReceivePreprocessSmeltLeachRemove impuritiesRecover metalsTreat residue

Decision model

A bounded question with a complete plant consequence.

Decision

Choose route settings and recycle policy that maximise value recovery without hiding reagent, water or residue burdens.

System boundary

Safe receiving and preprocessing abstraction through smelting, alloy/slag/gas treatment, leaching, impurity removal, product recovery and wastewater/residue treatment.

Governing structure

Equations and accounting rules

01Element-by-element mass balances
02Partition to alloy, slag and dust
03Leach stoichiometry and extraction yield
04Precipitation/selectivity plus recycle purge
Scenario set

Base, alternative and stress cases

  • NMC111/622/811 mix
  • Production scrap and high copper
  • Higher LFP share as boundary case
  • Lithium recovery, acid or water constraint

Engineering brief

Model the complete decision, not an isolated unit operation.

Umicore publicly describes a combined high-temperature smelting and hydrometallurgical refining architecture for nickel, cobalt, copper and lithium recovery.

Furnace chemistry, reagent recipes, yields and costs are proprietary. The model separates metallurgical yield from regulatory recovery accounting and treats feed chemistry as a scenario.

01 · Model basis

What the Acatian model needs to resolve

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

Inputs

Data

Li, Ni, Co, Mn, Cu, Al, Fe, C and moisture

Evidence

Furnace partition, flux and energy

Plant

Leach recovery and reagent stoichiometry

Basis

Selectivity, water recycle and product limits

Mechanisms

Balance

Element-by-element mass balances

Model

Partition to alloy, slag and dust

System

Leach stoichiometry and extraction yield

Time

Precipitation/selectivity plus recycle purge

Constraints

Limit

Feed chemistry and safe preprocessing

Risk

Furnace capacity and partition uncertainty

Capacity

Reagent, selectivity and impurity limits

Gate

Water recycle, residue and regulatory boundary

Outputs

Result

Recovered metal kg/t feed

Decision

Reagent, water and furnace energy

Plant

Product purity and residue tonnes

Value

Plant versus regulatory recovery and value proxy

02 · Acatian workflow

Build it in six controlled steps

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

    Characterise feed by element and phase.

  2. 02

    Close smelting partition balances.

  3. 03

    Model leach and impurity removal.

  4. 04

    Add selective recovery and recycle.

  5. 05

    Reconcile water, reagents and residues.

  6. 06

    Compare chemistry-mix robustness.

03 · Decisions

Questions the model should answer

Which feed mix remains valuable?

Where is lithium lost?

Which impurity drives reagent demand?

How much water recycle is stable?

04 · Evidence boundary

Validate before the result carries weight

Validation

Require element closure, declared salt/electroneutrality accounting, recycle convergence and comparison with authorised assay, residue and recovery evidence.

Limitations

The study is not a proprietary Umicore flowsheet, waste-classification decision or final plant design. Safety and environmental approval remain external.

Public evidence

What the company context supports—and what it does not.

Sources establish the public process architecture. They do not reveal private operating parameters, site performance or an Acatian relationship.
  1. Umicore — pyro-hydro technologyPublic combined smelting and chemical-refining architecture.
  2. EU Delegated Regulation 2025/606Regulatory recovery-accounting context.

Frequently asked questions

Practical modelling questions

Is this the named organisation's real plant model?

No. It is an independent hypothetical Acatian study based only on the cited public process architecture. It claims no affiliation, endorsement, deployment, confidential data or actual plant performance.

Where do the numerical inputs come from?

Every input must be marked as a public fact, literature estimate, transparent engineering assumption or authorised customer input. The public article does not invent private operating values.

Can the model be calibrated to a real facility?

Yes, when the operator supplies authorised process, equipment, schedule and utility evidence and agrees the intended use, acceptance criteria and validation plan.

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.