How it works

Technology · How it works

Unlocking copper the industry left behind

~70% of the world's copper sits in low-grade primary sulfide ores — chalcopyrite chief among them — stranded by a fundamental barrier that conventional leaching cannot overcome. Jetti's catalyst unlocks chalcopyrite, working within your existing heap and SX-EW infrastructure.

~70%
of global Cu resources in primary sulfides
~50 yr
industry tried and failed to solve chalcopyrite
No
special permits, plants, or mining method required
Foundation knowledge

Not all copper ore is created equal

Copper deposits contain three mineralogical families — each with fundamentally different chemistry, leachability, and extraction economics. Understanding the difference explains why low-grade primary sulfides remained stranded for decades.

Oxide ores

CuO · Cu(OH)₂ · CuCO₃

Oxide ores — malachite, azurite, chrysocolla — sit near the surface in the weathered zone. They dissolve readily in dilute sulfuric acid, making them ideal for standard heap leach → SX-EW processing. Well understood, low risk, and the historical foundation of the copper hydrometallurgy industry — but progressively depleting as shallow deposits are exhausted.

Heap leach amenability Excellent
Leaching speed Fast — weeks to months
Resource abundance ~15% of global Cu
Technology risk Low — fully proven
Standard extraction pathway — oxide ore
Mine & place on heap
ROM or crushed ore on lined leach pad
✓ Standard
H₂SO₄ irrigation
Acid dissolves Cu minerals directly and rapidly
✓ Highly effective
PLS → SX-EW → Cathode
Proven, mature processing circuit
✓ Proven
The core problem

Why chalcopyrite resisted for 50 years

Passivation is not a physical crust — it is an electrochemical phenomenon. The surface layer that forms during chalcopyrite leaching turns the mineral from a resistor into a diode, choking electron flow and halting copper dissolution. Our hypothesis: three mechanisms combine.

Select a state to visualise
CuFeS₂

Fresh chalcopyrite surface: ferric ions (Fe³⁺) attack the mineral. Electrons transfer freely from the n-type bulk mineral to the oxidant. Copper dissolves into solution — leaching proceeds normally in the early stages of a bioleach.

Our hypothesis: three mechanisms combine to block extraction

Our process

Five steps from ore to cathode

Jetti integrates into standard heap leach operations with minimal infrastructure changes. No flowsheet redesign, no special permits, no changes to the mining methods. Select each step to explore.

Step 1 — Ore placement

Chalcopyrite ore (Most common primary sulfide ore) — whether run-of-mine (ROM) or crushed material— is stacked onto a lined heap leach pad using existing conveying and stacking equipment. No changes to mining methods, blasting, or haulage are required. Jetti can be applied to new lifts on active pads, or to rehandled stockpile material, without interrupting production.

Low risk by design

Three pillars that protect your operation

Jetti's technology is built to integrate without disruption. Three independently tested properties — biocompatibility, reversibility, and SX/EW compatibility — mean your existing processes continue to perform exactly as they do today.

Biocompatible with iron-oxidizing bacteria

Tested across multiple temperatures — independent laboratory

Iron-oxidizing and sulfur-oxidizing bacteria are the engine of bioleaching — they regenerate the ferric oxidant that drives chalcopyrite dissolution. Jetti’s catalyst was specifically designed not to interfere with this biological system, and independent testing confirms this.

Confirmed: the Jetti catalyst does not negatively affect bio-oxidation.

Fully reversible — no legacy effects

Electrochemical and biological reversibility — independent laboratory confirmed

If a mine operator decides to stop catalyst addition — for any reason — the heap system returns to its pre-Jetti baseline. There are no irreversible changes to the mineral surface, the bacterial community, or the leach solution chemistry.

Removing the catalyst from the raffinate stops the electron-bridge effect immediately. Within a few cycles the surface layer reforms and leaching returns to its standard SHL kinetics. SX-EW chemistry is unaffected throughout.

Reversibility demonstrated in the heap circuit. Electrochemical response returns toward the pre-Jetti baseline after catalyst removal. Two independent impedance metrics are shown side by side for comparison.

Reversibility demonstrated in the heap circuit

Electrochemical response moves through passivation, de-passivation after catalyst removal, and re-passivation — two independent impedance metrics tracked over cumulative time.

Passivation
De-passivation
Re-passivation

After catalyst removal the response drops (de-passivation) and then recovers toward baseline (re-passivation), consistent with no persistent legacy effect.

No impact on SX, EW, or cathode quality

Independent third-party testing — lab and industrial scale

The catalyst circulates through the full leach circuit — which means it passes through the SX plant in every raffinate cycle. Significant testwork and current commercial operation confirm that the catalyst at heap concentrations does not detrimentally impact extraction efficiency, phase disengagement time, interfacial tension, electrolyte quality, or cathode grade.

Data from an operating Jetti site shows 100% A-grade cathode since implementation — with zero cathode quality rejections. EW pilot testing showed higher current efficiency in catalyzed conditions than in the control (94.1% vs 89.9%). No changes to organic consumption, no crud formation, no co-extraction of deleterious elements.

SX organic phase✓ No impact
Phase disengagement✓ No impact
Electrolyte quality✓ No impact
Cathode grade✓ No Impact
Mine rehabilitation plan✓ No changes
EW current efficiency↑ No Negative Impact
Digital intelligence

Rosetta — Column digital twin

Rosetta is Jetti's column digital twin — designed to simulate column testwork and support commercial decision-making. Built on more than 10 years of extensive testwork, it converts mineralogical data, catalyst dose, column conditions, and time into catalyst and control recovery trajectories. This serves as a quick, site-specific business case before a single tonne of ore is processed.

Live platformRosetta Neural Network
Cu recovery forecast — catalyzed vs. control
0255075100060120180240Cu recovery (%)Leach day
CatalyzedControl (SHL)
Try Rosetta with your oreRun a site-specific recovery forecast — free, no sign-in

Neural network ensemble model

Rosetta runs an ensemble of neural networks trained on 10+ years of column testwork. Each prediction includes a P20–P80 confidence band — a probabilistic recovery range, not a single point estimate.

User-configurable column inputs

Set irrigation rate, column height, P80, and column diameter. Rosetta converts these into internal model features before inference — no specialist expertise required.

Catalyzed vs. control — side by side

Every run outputs both the catalyzed ensemble mean and the control baseline on the same chart. The separation between the two curves is the traceable expected uplift under the specified conditions.

De-risking framework

A standardized ladder from lab to mine

Jetti's validation pathway is structured, sequential, and data-gated — each stage de-risks the next, and no commercial decision is made without the evidence to support it.

Reactor testwork

Phase 1 — Ore qualification

Reactor tests are rapid, small-scale experiments that evaluate ore samples for catalyst amenabilitiy before any investment in column infrastructure. Multiple ore types from a single site can be tested in parallel — characterising mineralogical variability and identifying the most amenable ore domains.

Typically available within 12–16 weeks of sample receipt.

Flexibility: an industrial-scale trial can be initiated after reactor testwork — or run in parallel with columns — depending on the level of risk-reward appetite of the operator. This decision is made jointly with Jetti.
Fine grind (75–106 μm)
Control vs. catalyzed runs in duplicates, and Cu, Fe, OPR, bacteria and ORP are monitored

Column testwork

Phase 2 — Heap simulation

Column tests simulate heap leach conditions at a scale that captures mass transfer, permeability, and solution channelling effects absent in reactor tests. Crushed ore at representative P80 is packed into columns, irrigated at site-representative rates.

All columns are run in duplicate with matched control and catalyzed pairs under identical conditions. Batch SX is performed independently on each column PLS using site-sourced organic — confirming SX/EW compatibility before commercial deployment.

ROM and crushed configurations tested in parallel
Site raffinate or synthetic lixiviant as liquid feed
Aeration matching site specifications
Batch SX with site-sourced organic
ORP, pH, Cu, Fe, catalyst concentration monitored weekly
Duplicate columns per condition — statistical rigor on uplift

Industrial trial

Optional — risk-reward decision

In some cases, operators prefer to move directly from reactor testwork to an industrial-scale trial — either instead of, or in parallel with, column testwork. This is a commercial and operational decision made jointly with Jetti, based on the operator's risk appetite, site conditions, and strategic timeline.

It provides early production upside while simultaneously de-risking the technology under site-specific conditions.

Can be initiated after reactor testwork, or run alongside columns
KPIs agreed upfront — same performance-linked commercial framework as full deployment
Jetti in a Box dosing unit deployed — minimal site modification
Real-time monitoring: ORP, Cu, catalyst concentration, flow
When an industrial trial makes sense
High confidence from reactor data
Operator wants early production
Fast-track
Parallel to column testwork
Industrial trial runs simultaneously — columns provide detailed kinetics, trial provides commercial data
Parallel
Risk-reward decision with Jetti
Timeline, ore confidence, and commercial appetite determine the right sequencing
Joint decision
Fully reversible
Stop dosing at any time — heap returns to baseline with no legacy effects
Zero lock-in

Industrial deployment

Phase 3 — Commercial operation

Commercial deployment requires minimal site modification. Jetti's compact dosing unit connects to the existing raffinate line — the only tie-ins required are a raffinate source, an electricity connection, and a water line. No changes to the SX plant, leach pad geometry, or downstream processing are needed.

Performance KPIs are agreed with the site operator before deployment and govern the commercial relationship. Jetti monitors all KPIs in real time through an integrated data system.

Dosing unit connects to raffinate line, power, and water only
KPIs defined before deployment
Jetti field team on-site for saturation and ramp-up phase
Real-time telemetry — ORP, Cu, catalyst concentration, flow rate
No interruption to existing mine operations during deployment
Deployment integration — tie-in points only
SX raffinate return line
Catalyst dosed into existing raffinate stream
Tie-in
Existing drip / sprinkler system
Catalyzed raffinate irrigated — no infrastructure changes
Standard
Real-time KPI monitoring
ORP, Cu, Fe, catalyst — Jetti data platform
Live
SX-EW — same plant
Higher Cu in PLS → higher cathode output from existing assets
Uplift
Ready to evaluate your site?

Start with your ore. We'll model the rest.

Jetti’s standardized assessment process begins with a sample request and a site information questionnaire. Most sites receive a go / no-go recommendation within 12 weeks of sample receipt.

Request an assessment