Skip to content

INDUSTRIAL WATER TREATMENT

Validate with real water.
Decide with operating evidence.

Nano-Fe heterogeneous complexation for selected PCB, rare-earth and electronic copper-foil wastewater streams, from sample screening to bypass pilot and engineering coordination.

Representative-water testingModular 1–5 m³/h pilotEffluent + total-cost review

PRIORITY STREAMS

Start with the stream
that changes the decision.

High-value metals should be recovered first. The platform is assessed for complexed or residual streams where polishing, stability or reuse risk remains.

01 / PCB

Complexed copper and nickel

Electroless copper, surface-treatment and related segregated streams. Review total Cu/Ni, COD or TOC, reagent use, dry solids and continuous stability.

02 / RARE EARTH

Fluoride and multi-metal tailwater

Assess high-salt competition, fluoride, phosphorus, residual metals and rare-earth constituents after recovery steps.

03 / COPPER FOIL

Polishing before reuse

Focus on residual metals, turbidity or SDI, membrane impact, cleaning frequency and the treatment-cost basis.

TECHNOLOGY

Transfer contaminants
to a separable solid phase.

Active iron oxyhydroxide surfaces support heterogeneous complexation, adsorption and co-precipitation. Conditions must be confirmed against representative water.

  1. 01

    Characterise

    Map water source, speciation, coexisting ions and the current process.

  2. 02

    Screen

    Test capture, controlled oxidation where relevant, and solid-liquid separation.

  3. 03

    Pilot

    Run a matched bypass comparison and optimise operating parameters.

  4. 04

    Define

    Confirm the design envelope, acceptance basis and implementation boundary.

MODULE ARCHITECTURE

Make every process interface
visible before fabrication.

This functional diagram shows the review sequence, not the final project arrangement. Module size, materials and interfaces are confirmed against the design envelope.

Sizing basis
Flow range × operating hours × contaminant load
Materials
Confirmed against pH, salinity, oxidants and site conditions
Controls
pH, ORP, flow and turbidity; optional project-specific interfaces
Handover
P&ID/interface list, operating parameters and acceptance basis

7 + 30 + 90

Validation before
engineering commitment.

Indicative stages only. Timing depends on sample availability, site conditions and the continuous-run plan.

ABOUT 7 DAYS

Sample diagnosis

Water analysis, bench screening, initial reagents and a pilot recommendation.

ABOUT 30 DAYS

Bypass pilot

Matched influent comparison, stability, reagents, energy, solids and reuse impact.

ABOUT 90 DAYS

Continuous demonstration

Operating variability, start-stop events, design envelope and commercial handover basis.

What we do not promise before validation

No fixed removal result, cost reduction or payback period is claimed without a representative-water test and agreed operating conditions. Cyanide-bearing, radioactive or other specialised streams require separate assessment and qualified implementation.

NEXT STEP

Prepare the pilot brief.

Organise water-quality data, the current process, cost baseline and site conditions before the first technical review.

Open the application pack ↗