Inside Ivanhoe Electric's Santa Cruz Copper Project: A Deep Dive into Heap Leach & SX/EW Processing

Overview

Nestled in the mineral-rich landscape of Arizona, the Santa Cruz Copper Project represents a significant and modern endeavor in the United States’ critical minerals strategy. Operated by Ivanhoe Electric Inc., this advanced-stage project is poised to become a major domestic supplier of high-purity copper cathode, a commodity crucial for the electrification of the economy and renewable energy technologies. Located in the renowned Arizona Copper Belt, the project leverages a substantial resource base estimated at 136 million tonnes of ore, with a life-of-mine plan extending over 24 years. The processing methodology selected for this deposit is a sophisticated, yet proven, heap leach combined with solvent extraction and electrowinning (SX/EW) circuit, designed specifically for the oxide and secondary sulphide ore types present. This approach was chosen for its efficiency, lower energy intensity compared to conventional concentrator-flotation-smelter routes, and its ability to produce LME Grade A copper cathode directly on-site. The project, as outlined in its recent NI 43-101 Feasibility Study, is designed for a substantial throughput of 22,000 tonnes per day, targeting an impressive overall copper recovery of 92.2%. The Santa Cruz project is not just another mining operation; it is a strategically important asset designed to address the growing domestic copper shortage with a focus on sustainability and operational excellence, making it a key project to watch in the coming decade.

Key Process Stages

The Santa Cruz Copper Project employs a meticulously designed mineral processing circuit that transforms run-of-mine ore into high-purity copper cathode. The flow sheet is a conventional yet optimized sequence of size reduction, agglomeration, leaching, and solution purification. The entire operation is designed for 24/7/365 operation, with specific annual operating hours allocated to different sections: 6,570 hours for crushing and agglomeration and 8,497 hours for the continuous SX/EW plant. The following bullet points detail each critical stage of this advanced copper processing circuit.

  • Stage 1: Primary Crushing Run-of-mine ore, delivered to the surface via a Railveyor system at a size of sub-20 cm, is first fed to a vibrating grizzly feeder. A magnet and metal detector remove tramp metal before the ore enters a single C160 Jaw Crusher for primary size reduction. Grizzly undersize bypasses the crusher to improve efficiency.
  • Stage 2: Secondary and Tertiary Crushing The primary crusher discharge combines with grizzly undersize and is fed to an MP1000 cone crusher operating in open circuit. The product then moves to a closed-circuit tertiary crushing stage featuring two parallel MP1000 cone crushers and two double-deck banana screens (3m x 6.7m). The circuit is designed to produce a final product size of 100% passing 9.5 mm, which is conveyed to truck loadout hoppers.
  • Stage 3: Agglomeration and Stacking The crushed ore is trucked to the leach pad area where it is fed into one of two portable agglomeration drums. Here, key reagents are added: sulphuric acid (6 kg/t) and sodium chloride (1 kg/t) to facilitate particle bonding and enhance leaching kinetics. The agglomerated ore is then systematically stacked onto the on/off leach pad in a 6-meter-high single lift using a mobile conveyor system culminating in a radial stacker.
  • Stage 4: On/Off Heap Leaching The leach pad consists of seven cells (each 130m x 640m), constructed with a composite liner system for environmental protection. Each cell undergoes a precise 265-day cycle: 36 days of stacking, 180 days of irrigation with raffinate solution at a rate of 8 L/h/m², and additional time for drainage and setup. Air is forced into the base of the heap via fans to aid in oxidizing secondary sulphides. Pregnant Leach Solution (PLS) reporting an average of 2,000 m³/h is collected and pumped to the SX plant.
  • Stage 5: Solvent Extraction (SX) The PLS enters a two-train SX circuit. Each train consists of two extraction stages, two wash stages, and one strip stage. A specialized organic extractant selectively removes copper from the aqueous PLS in mixer-settlers. The copper-loaded organic is then stripped using lean electrolyte from the EW circuit, producing a rich electrolyte solution that is filtered to remove organic carryover before being sent to electrowinning.
  • Stage 6: Electrowinning (EW) The rich electrolyte is pumped into an electrowinning tankhouse containing 124 cells, each holding 84 stainless-steel cathode blanks. Using two powerful rectifiers (67 kA / 287 V), an electrical current plates copper onto the blanks. The resulting LME Grade A copper cathodes are harvested, stripped, washed, bundled, and prepared for shipment.
  • Stage 7: Spent Ore Management After leaching, spent ore is removed from the pad. Approximately 50% is transported to a paste backfill plant for use underground, while the remainder is trucked to one of two engineered, lined spent ore storage facilities for permanent disposal, following strict environmental guidelines.

Critical Data

The feasibility of the Santa Cruz Copper Project is underpinned by robust metallurgical testwork and detailed engineering, resulting in the following key performance indicators and design criteria.

Parameter Value Unit Notes
Throughput (Stacking Rate) 22,000 t/d Design daily stacking rate to leach pad
Life-of-Mine Ore Production 136 Mt Total ore to be processed over 24 years
Target Grind Size (Crush Size) 9.5 mm (P100) 100% passing 9.5 mm after tertiary crushing
Overall Copper Recovery 92.2 % Life-of-mine average recovery to cathode
Design Annual Copper Production 76,000 t/y Target annual cathode production
Acid Consumption 6 kg/t ore Sulphuric acid addition at agglomeration
Irrigation Rate 8 L/h/m² Applied to the heap leach surface
Bond Work Index (Spent Ore) 14.9 kWh/t For paste backfill design considerations
Crusher Work Index 4.0 kWh/t For crushing circuit energy calculations

Additional Interesting Data and Summary

Beyond the core processing circuit, the Santa Cruz Copper Project incorporates several advanced features that highlight its modern design and commitment to sustainability. The project is designed as a zero-discharge facility, a critical aspect of its water management strategy in arid Arizona. Makeup water is sourced from a combination of grandfathered water rights and mine dewatering, with the latter being treated and also supplied to local agricultural users, showcasing a community-focused approach to resource sharing. The solution management system is extensive, comprising multiple lined ponds (Raffinate, PLS, SLS, and stormwater) sized to handle both process flows and a 100-year, 24-hour storm event, ensuring environmental protection.

The project’s energy footprint is a key consideration. The use of a heap leach-SX/EW process is significantly less energy-intensive than traditional smelting, and the design includes efficient crushing equipment with specific work indices well-characterized for accurate power forecasting. The electrowinning tankhouse is equipped with cell covers and mist suppression systems to minimize acid mist emissions and ensure worker safety, aligning with best practices for industrial hygiene.

Economically, the project is substantial, with a projected annual production of 76,000 tonnes of copper cathode, directly contributing to the US copper supply chain. The spent ore management plan is innovative, diverting half of the material to become paste backfill underground, which reduces surface waste storage requirements and improves the geotechnical stability of the mined-out voids. The detailed NI 43-101 report underscores the project’s viability and positions Ivanhoe Electric as a significant future player in the copper market, leveraging smart mineral processing technology to develop a high-quality deposit responsibly.

Source: NI 43-101 Technical Report | Feasibility | Project: including resource estimation on copper deposit | Date: June 2025

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