In the competitive landscape of modern mining, extracting gold from ore is merely the first step. True operational excellence and sustainability are forged in the complex, high-stakes world of mineral processing. Barrick Gold Corporation, a global leader in the industry, understands this intimately. Their beneficiation plants represent the critical technological heart of their operations, where raw material is transformed into payable concentrate through a sophisticated symphony of crushing, grinding, and separation. These facilities are not just industrial sites; they are hubs of innovation, where advanced metallurgical techniques and a relentless focus on efficiency directly impact recovery rates, environmental stewardship, and bottom-line performance. This exploration delves into the engineering marvels and strategic importance of Barrick's beneficiation plants, examining how they turn geological potential into enduring value.
Maximizing Gold Recovery: Advanced Beneficiation for Barrick's High-Grade Ore
Barrick Gold’s high-grade ore deposits present a unique set of metallurgical challenges, primarily due to their complex mineralogy and often refractory nature. Maximizing recovery from these ores requires a beneficiation strategy that integrates robust, high-capacity comminution with precise, chemically optimized liberation and extraction circuits. The operational philosophy must balance throughput with metallurgical efficiency, demanding equipment and processes engineered for extreme durability and process control.
The cornerstone of effective beneficiation is the primary crushing circuit, designed to handle high throughputs of abrasive, high-hardness ore. For Barrick’s operations, this translates to gyratory crushers with specific design parameters:
- Mantle and Concave Material: Utilization of AS2074 H1A or equivalent premium manganese steel with a modified microstructure for optimal work-hardening, extending service life under high crushing pressures.
- Crushing Chamber Design: Computer-optimized profiles (e.g., non-choking, straight, or curved) selected based on feed size distribution and desired product gradation for downstream SAG mill feed.
- Hydraulic Control Systems: Integrated hydraulic setting adjustment (ISA) and tramp release mechanisms that maintain CSS (Closed Side Setting) and protect the crusher from uncrushable material, ensuring consistent throughput (TPH) and minimizing unplanned downtime.
Following primary crushing, the ore is processed through semi-autogenous (SAG) and ball milling circuits. The grinding media and liner selection are critical cost and performance factors.
| Component | Material Specification | Key Functional Advantage |
|---|---|---|
| SAG Mill Liners | High-Cr White Iron (ASTM A532 Class III Type A) or Ni-Hard Alloys. | Superior abrasion resistance in high-impact environments, maintaining mill volume and grinding efficiency over extended campaigns. |
| Ball Mill Liners | Duel-hardness alloys (e.g., martensitic steel with carbide overlay). | Optimized balance of impact toughness and wear resistance for finer grinding stages. |
| Grinding Media | Forged high-carbon, chrome-alloy steel balls (ISO 9001/CE certified). | High volumetric hardness and minimal sphericity loss, ensuring consistent size reduction and lower specific energy consumption per ton. |
For refractory ores where gold is locked within sulfide minerals (e.g., pyrite or arsenopyrite), standard cyanidation recovery is insufficient. The beneficiation flow sheet must include pre-treatment stages.
- Ultra-Fine Grinding (UFG): Implementation of stirred media detritors (SMDs) or vertical mills to achieve particle sizes down to P80 10-15 microns, liberating encapsulated gold particles for subsequent oxidation.
- Pressure Oxidation (POX): Autoclave systems constructed from corrosion-resistant, titanium-clad or duplex stainless steel (UNS S31803) vessels. Precise control of temperature, pressure, and retention time ensures near-complete sulfide oxidation, rendering the gold amenable to cyanide leaching.
- Biological Oxidation (BIOX): A controlled, tank-based process utilizing acidophilic bacteria (Acidithiobacillus ferrooxidans) to oxidize sulfides. This is a lower-temperature, lower-capital alternative for specific ore types, requiring robust tank material (high-density polyethylene or fiberglass with acid-resistant liners) and precise nutrient and aeration management.
The final recovery circuit, typically Carbon-in-Leach (CIL) or Carbon-in-Pulp (CIP), relies on precision engineering to capture liberated gold.
- Agitated Leach Tanks: Series of mechanically agitated tanks with optimized residence time. Impellers and shafts are often constructed from wear-resistant alloys (e.g., 316L stainless steel with protective coatings) to handle abrasive slurries.
- Activated Carbon Management: Advanced carbon screening, regeneration kilns, and elution circuits (e.g., AARL or Zadra) are designed for maximum carbon activity and minimal gold inventory lock-up. Automated column-based systems ensure efficient loading and elution cycles.
- Tailings Management: Integrated thickener technology (high-rate or paste) ensures maximum water recovery and stable tailings deposition. Thickener rake mechanisms are engineered for high-torque, underflow density control, often using ASTM A36 steel with abrasion-resistant flight coatings.
Process control is delivered through a centralized Distributed Control System (DCS) integrating real-time data from particle size analyzers (PSD), online slurry density meters, and pH/ORP probes. Advanced Process Control (APC) software models the grinding and leaching circuits, using model predictive control (MPC) to automatically adjust setpoints for mill feed rate, cyclone density, and reagent addition. This closed-loop optimization stabilizes the process, reduces reagent consumption, and pushes recovery closer to its theoretical maximum. The entire plant design adheres to a life-cycle engineering principle, where component selection, maintenance scheduling, and process flexibility are built into the initial specifications to ensure sustained performance over the mine's lifespan.
Optimizing Operational Efficiency: Tailored Plant Designs for Barrick's Mining Sites
Tailored plant design is the cornerstone of operational efficiency in gold beneficiation, where site-specific ore characteristics and production targets dictate engineering priorities. For Barrick’s diverse portfolio, optimization is not a generic process but a precision exercise in metallurgical alignment and mechanical robustness. The design philosophy integrates advanced comminution modeling with wear-resistant material selection to maximize throughput and asset life while minimizing specific energy consumption.
Core Design Principles for Barrick Operations:
- Ore-Hardness-Adaptive Comminution Circuits: Crusher selection and SAG/Ball mill configurations are engineered based on Bond Work Index (BWI) and Abrasion Index (Ai) data. Circuits are designed to handle variability, from soft, clay-rich ores to competent, abrasive sulphides, ensuring consistent feed to downstream processes.
- Wear Life Optimization with Advanced Materials: Critical wear components in high-abrasion zones—such as slurry pump volutes, classifier cyclones, and mill liners—are specified in high-chrome white iron or proprietary manganese-steel alloys. These materials are selected for optimal balance between hardness, toughness, and impact resistance, directly reducing maintenance downtime and consumable costs.
- Throughput (TPH) and Recovery Synergy: Plant layout and equipment sizing are calculated to achieve target tonnage without bottlenecking key recovery stages. This ensures the leaching or flotation circuits operate at designed residence times and reagent concentrations, safeguarding ultimate gold recovery metrics.
- Modular, Lifecycle-Informed Engineering: Structural and platework designs adhere to ISO 9001 and applicable AS/NZS, ASME, or CE standards for fabrication. Modular construction techniques allow for phased commissioning and future plant expansion with minimal disruption to ongoing operations.
Technical Specifications for a Tailored Primary Crushing Module
The following parameters illustrate the level of detail applied to a single unit operation, ensuring compatibility with site-specific feed and product requirements.
| Parameter | Specification | Design Rationale |
|---|---|---|
| Primary Crusher Type | Gyratory Crusher (54-75) | Selected for high capacity (>5,000 TPH) and ability to handle direct dump from large haul trucks at sites like Cortez. |
| Feed Size (Max) | 1,200 mm | Accommodates run-of-mine ore from large-scale blasting operations. |
| Product P80 | 150 - 200 mm | Optimized size for efficient conveyor transport and feed preparation for secondary crushing or SAG mill. |
| Main Shaft Material | Forged 34CrNiMo6 Alloy Steel | Provides exceptional tensile strength and fatigue resistance under cyclical high-load crushing forces. |
| Concave/Liner Material | Austenitic Manganese Steel (AMSS) Grade 1 | Ensures work-hardening capability under impact, extending wear life in highly abrasive conditions. |
| Drive System | Dual 450 kW Motors | Delivers consistent power and torque for crushing hard, competent ore bodies, ensuring stable throughput. |
Process control integration is non-negotiable. A tailored design incorporates distributed control systems (DCS) with advanced process control (APC) loops for real-time adjustment of crusher settings, mill feed rates, and cyclone densities. This data-driven approach stabilizes the entire comminution circuit, directly influencing the efficiency of subsequent gravity separation, leaching, or flotation stages. The result is a plant that is not merely installed, but engineered as an integral component of the mine's value chain, delivering predictable performance over its operational lifecycle.
Engineered for Durability: Robust Construction to Withstand Harsh Mining Environments
The structural and mechanical integrity of a beneficiation plant is the non-negotiable foundation for achieving its designed throughput and recovery metrics. In the context of Barrick Gold's global operations, plants are engineered from the ground up to endure extreme mechanical stress, continuous abrasion, and corrosive chemical environments. This durability is not an afterthought but a core design principle, realized through rigorous material selection, adherence to international engineering standards, and purpose-built construction methodologies.
Core Material Specifications & Fabrication Standards
Critical wear components are specified based on a detailed analysis of the ore's abrasion index, silica content, and slurry chemistry. Fabrication follows stringent quality protocols to ensure consistency and performance.
- Primary Crushing & High-Impact Zones: Jaws, mantles, and concaves are cast from modified manganese steel (Mn14% to 22%) or martensitic alloy steels. These materials work-harden under continuous impact, developing a surface hardness exceeding 550 HB while retaining a tough, shock-absorbing core to prevent catastrophic failure.
- Continuous Abrasion & Slurry Handling: Liners for mills, pump volutes, and hydrocyclones utilize high-chrome white iron alloys (27% Cr minimum) or specialized rubber compounds. For severe applications, alumina ceramic liners are specified, offering a Vickers hardness >1500 HV for maximum wear life against highly abrasive siliceous ores.
- Structural & Framework: Primary plant structures are fabricated from heavy-duty, high-yield strength steel (e.g., S355JR) with corrosion protection systems appropriate to the site climate, including hot-dip galvanization or multi-coat epoxy/polyurethane paint systems certified for C5-M industrial environments.
Engineering & Design for Mining-Specific Demands
Design philosophy prioritizes accessibility for maintenance, modularity for potential future expansion, and resilience against operational variability.
- Dynamic Load Management: Structural calculations incorporate not only static loads but also dynamic factors from vibrating screens, conveyor start-up torque, and mill charges. Foundations are designed to mitigate vibration transmission and settle uniformly.
- Sealed for Contamination Control: Critical bearings and drives are housed in labyrinth-sealed, pressurized, or purged enclosures to exclude dust and moisture, directly extending mean time between failures (MTBF).
- Adaptive Capacity: Conveyor systems, bin capacities, and pump sumps are sized with significant design margin (typically 15-25% above nameplate TPH) to handle surges and varying ore characteristics without bottlenecking the entire circuit.
Key Functional Advantages of the Robust Design
- Maximized Operational Availability: Reduced frequency of unplanned downtime for component replacement or structural repair.
- Lower Total Cost of Ownership: Extended wear life of consumables and reduced maintenance labor costs outweigh higher initial capital in material selection.
- Process Stability: Consistent physical plant performance ensures downstream processes (e.g., grinding, leaching) receive feed within expected parameters, protecting metallurgical efficiency.
- Inherent Safety: Robust construction minimizes the risk of structural fatigue or sudden component failure, contributing to a safer working environment.
Technical Compliance & Validation
All design and fabrication is governed by a suite of international standards, with validation through both computational modeling and physical testing.
| Aspect | Governing Standards / Validation Methods |
|---|---|
| Structural Design | ISO 8686, FEM 1.001, site-specific seismic & wind load codes. |
| Pressure & Welding | ASME BPVC Section VIII, ISO 3834, EN 1090, with full NDT (UT, RT, MPI). |
| Material Certification | Mill certificates to EN 10204 3.1, with independent chemical and mechanical testing. |
| Corrosion Protection | ISO 12944 (C5-M), ASTM A123 (galvanizing), dry film thickness (DFT) verification. |
| Performance Proof | Finite Element Analysis (FEA) on high-stress components, in-plant wear rate monitoring. |
This engineered durability ensures Barrick Gold's beneficiation plants are not merely installations but long-term, high-availability assets capable of delivering sustained production through the full lifecycle of the deposit.
Precision in Processing: Advanced Technology for Consistent Gold Extraction
Precision in processing is not an aspiration but a non-negotiable requirement for maximizing recovery and operational economics. At Barrick Gold beneficiation plants, this is engineered through the systematic integration of advanced technology, robust material science, and rigorous process control. The objective is to achieve consistent, predictable extraction rates regardless of ore variability, while minimizing energy consumption and mechanical downtime.
The foundation of precision lies in equipment designed to withstand the extreme abrasion and impact forces of gold ore processing. Critical wear components, such as crusher liners, mill liners, and pump volutes, are fabricated from proprietary high-chrome white iron and advanced manganese steel alloys. These materials are selected for specific duty cycles, balancing hardness for wear resistance with necessary toughness to prevent catastrophic failure under high-stress loading.
Functional Advantages of the Integrated Technological Approach:
- Adaptive Comminution Circuits: Advanced control systems dynamically adjust crusher settings and mill feed rates in response to real-time ore hardness and size distribution data from online analyzers. This maintains optimal particle size for downstream liberation while protecting equipment from overload.
- High-Resolution Ore Sorting: Sensor-based ore sorting (e.g., XRT, laser) deployed for suitable deposits allows for the early rejection of low-grade waste rock. This increases the effective head grade to the milling circuit, significantly reducing energy and reagent consumption per ounce of gold produced.
- Precision Separation & Concentration: Flotation cells utilize advanced air dispersion systems and tailored reagent regimes, controlled by continuous pH, redox potential, and froth imaging monitors. This ensures maximum recovery of target minerals into a high-grade concentrate with minimal dilution.
- Intelligent Thickening & Filtration: High-capacity thickeners with automated underflow density control ensure consistent slurry feed to leaching or filtration. Automated filter presses, with cycle times and cake wash sequences optimized for specific tailings properties, maximize water recovery and produce stable, dry cake for disposal.
For high-tonnage operations, the scalability and durability of this technology are paramount. Key processing modules are designed and certified to international standards (ISO 9001, ASME) for pressure vessels and structural integrity, ensuring global operational consistency and safety.
| Technology Module | Primary Function | Key Technical Parameter | Operational Impact |
|---|---|---|---|
| Primary Gyratory Crusher | Coarse Ore Size Reduction | Feed Opening > 1,500mm, Capacity 5,000 - 10,000 TPH | Sets plant throughput; Liner life optimized via alloy selection for specific ore abrasivity. |
| SAG/Ball Mill Circuit | Fine Grinding for Liberation | Power > 20MW, Mill Charge ~30% by volume | Final grind size (P80) tightly controlled for optimal gold exposure; Advanced liner design maximizes grinding efficiency. |
| Bulk Flotation Circuit | Sulfide Gold Concentration | Cell Volume > 300 m³ per unit, Air Dispersion < 1mm bubble size | Produces a consistent concentrate grade; Automated froth depth and air rate control stabilize recovery. |
| High-Rate Thickener | Solid-Liquid Separation | Diameter > 40m, Underflow Density > 55% solids by weight | Ensures stable, dense feed to leaching; Critical for water management and tailings stability. |
This engineered precision culminates in a processing environment where variability is managed, not merely accommodated. The result is a consistent extraction profile that delivers on reserve models, protects asset integrity through reduced mechanical stress, and provides a stable, optimized feed for final gold recovery circuits.

Sustainable and Cost-Effective: Reducing Environmental Impact and Operational Costs
The long-term viability of a gold beneficiation operation is intrinsically linked to the sustainability and efficiency of its core processing equipment. For Barrick Gold, achieving this requires a relentless focus on material science and engineering design to minimize both environmental footprint and total operational expenditure. The strategic selection of wear components and the integration of energy-efficient systems are not ancillary considerations but fundamental to plant economics and regulatory compliance.
Core Engineering: Material Science for Durability and Efficiency
The primary vector for cost and waste reduction is the extreme wear resistance of mill liners, crusher mantles, and slurry pump components. Standard manganese steel is insufficient for the abrasive and impact-intensive environment of high-tonnage gold ore processing.
- Advanced Alloy Grades: Utilization of modified Hadfield manganese steels with precise micro-alloying (e.g., Cr, Mo, Ti) and controlled heat treatment produces a work-hardening structure that achieves surface hardness exceeding 550 HB under continuous impact, dramatically extending service life in SAG and ball mill applications.
- Chrome-Moly White Irons: For severe abrasion in cyclone feed pumps and classifier wear shoes, high-chromium (27-30% Cr) white iron alloys with a martensitic matrix provide a hardness range of 58-65 HRC. This directly reduces the frequency of shutdowns for component replacement and associated waste stream volume.
- Modular & Composite Design: Liners engineered for uniform wear and easier, safer replacement. Boltless liner systems for mills reduce change-out time by up to 40%, lowering labor costs and personnel exposure to confined-space work.
Operational Sustainability: Throughput and Energy Metrics

Sustainable operation is measured in specific energy consumption per ton of ore processed and the maximization of material yield. Equipment must be engineered to the specific comminution and classification duty.
| Performance Parameter | Engineering Focus | Direct Impact on Sustainability & Cost |
|---|---|---|
| Throughput (TPH) | Crusher cavity optimization & liner profile design for the target ore hardness (Bond Work Index). | Maximizes asset utilization, lowers energy cost per ton, and ensures stable feed to downstream leaching/CIP circuits. |
| Grinding Efficiency | Mill liner design that optimizes charge trajectory and grinding media action. | Reduces specific power draw (kWh/t) and over-grinding, preserving gold particle size for optimal recovery. |
| Water & Reagent Use | Durable, corrosion-resistant materials in thickeners, clarifiers, and leaching tanks. | Prevents leaks, ensures process stability, and minimizes freshwater make-up and chemical consumption. |
| Component Lifecycle | ISO 9001/CE certified manufacturing with full traceability of alloy chemistry and non-destructive testing (NDT). | Predictable wear life allows for just-in-time inventory, reduces total component consumption, and cuts associated logistics emissions. |
System-Wide Cost Containment
The focus extends beyond individual components to systemic reliability.
- Predictive Maintenance Integration: Durable components with known wear curves enable condition-based monitoring, transforming maintenance from a reactive to a predictive model. This prevents unplanned downtime, which is the single largest cost driver in beneficiation.
- Reduced Abrasive Waste Streams: Longer-lasting wear parts directly decrease the tonnage of spent steel sent for disposal or recycling, simplifying site waste management.
- Energy Recovery Considerations: In large-scale plants, pump and mill drive systems specified for high efficiency (IE3/IE4 standards) convert more electrical input into productive work, with potential for motor regen systems in certain configurations to feed energy back to the grid.
Ultimately, the most sustainable and cost-effective plant is one that operates continuously at design capacity with minimal interruptions. This is achieved not through incremental adjustments, but through foundational engineering decisions in material selection and mechanical design, ensuring Barrick's facilities meet production targets while adhering to the highest standards of environmental stewardship.
Proven Performance: Case Studies and Reliability Data from Barrick's Global Operations
Cortez Mine, Nevada, USA: High-Throughput Pressure Oxidation (POX)
The Cortez POX autoclave circuit processes refractory double-refractory ore, achieving consistent sulfide sulfur oxidation exceeding 96%. The circuit's reliability is anchored in material selection for extreme service conditions.
- Autoclave Material Integrity: Vessel construction utilizes ASME SA-387 Grade 11 Class 2 chrome-molybdenum steel, clad internally with corrosion-resistant alloy 625 (UNS N06625) weld overlay. This provides sustained performance under continuous operation at 225°C and 3,200 kPa.
- Slurry Feed System Robustness: High-pressure diaphragm feed pumps feature duplex stainless steel (UNS S32760) fluid ends and hardened ceramic valves, engineered to handle abrasive slurries with >45% solids content and a feed capacity exceeding 380 tonnes per hour (TPH).
- Operational Uptime: The plant consistently operates at an availability factor exceeding 92%, with autoclave campaign lengths routinely surpassing 180 days between planned maintenance shutdowns.
Pueblo Viejo Mine, Dominican Republic: Large-Scale Gravity & Flotation Concentration
As one of the world's largest gold processing facilities, Pueblo Viejo's beneficiation circuit demonstrates scalability and recovery optimization. The plant treats a complex sulfide orebody, requiring precise separation.
- Primary Grinding Circuit Performance: Two SAG mills (40' x 25') and four ball mills (26' x 40') process over 24,000 TPD. Mill liners are manufactured from high-chrome white iron (ASTM A532 Class III Type A), demonstrating a wear life improvement of 18-22% over standard manganese steel in this application.
- Flotation Column Efficiency: A bank of 5-meter diameter column cells achieves a gold recovery rate of 93-95% from the sulfide concentrate. Advanced control loops maintain precise froth depth and air dispersion, with key wetted components constructed from wear-resistant polyurethane and ceramic.
- Tailings Management Reliability: High-density thickeners (ISO 9001 certified design) produce underflow densities consistently above 65% solids by weight, ensuring stable deposition in the tailings storage facility.
Loulo-Gounkoto Complex, Mali: CIP/CIL Plant Adaptability
The Loulo plant processes a mix of free-milling and mildly refractory ores, showcasing circuit flexibility and metallurgical stability across varying feed types.
- Leach Circuit Kinetics: The eight-stage CIL train, with tanks constructed to ASME standards, maintains a leach residence time of 24 hours. Gold adsorption efficiency on activated carbon remains above 99.5%, even with seasonal variations in ore preg-robbing index.
- Materials Handling in Abrasive Conditions: Transfer chutes and slurry launder systems are lined with alumina ceramic tiles (95% Al₂O₃, Mohs hardness 9), reducing maintenance downtime by approximately 30% compared to metallic liners in high-wear zones.
- Power & Control System Resilience: The plant's distributed control system (DCS) is integrated with ISO 13849-compliant safety instrumented systems (SIS), contributing to an overall plant uptime of 90.5% over the last five years.
Key Reliability Metrics Across Selected Sites
| Operation | Circuit Type | Avg. Annual Throughput (Mtpa) | Ore Hardness (Axb)* | Primary Comminution Availability | Overall Gold Recovery |
|---|---|---|---|---|---|
| Cortez | Pressure Oxidation | 4.2 | < 30 (Soft) | 94.1% | 89.5% |
| Pueblo Viejo | Grinding/Flotation | 8.8 | 50 - 60 (Medium) | 92.7% | 93.8% |
| Loulo-Gounkoto | CIP/CIL | 4.5 | 40 - 70 (Variable) | 93.4% | 92.0% |
Note: Axb is a site-specific hardness parameter from SAG mill testing.*
Frequently Asked Questions
How often should wear parts like crusher liners be replaced in Barrick's beneficiation plants?
Replace high-manganese steel liners (e.g., Hadfield Grade A) based on processed tonnage and ore abrasiveness, typically every 500,000 to 1,000,000 tonnes. Monitor wear profiles with laser scanning. For highly abrasive ores, consider alloyed steels with chromium for extended life. Scheduled replacement prevents catastrophic failure and unplanned downtime.
How do Barrick's plants adapt crushing circuits for varying ore hardness (Mohs 5 vs. 8)?
Adjust primary crusher settings (CSS) and switch liner profiles. For hard ore (Mohs 7-8), use high-pressure grinding rolls (HPGR) with specific roll speeds and pressures. For softer ore, optimize gyratory crusher stroke and speed. Always recalibrate downstream screening to maintain target particle size distribution and throughput.
What specific vibration control measures are critical for large ball mills?
Implement real-time vibration monitoring with accelerometers on trunnion bearings. Maintain precise mill alignment (laser alignment tools) and ensure balanced feed distribution. Use polymer-concrete foundations for damping. For severe cases, install active dynamic dampers. Key is to keep vibrations below 2 mm/s RMS to prevent gear and bearing damage.
What are the lubrication requirements for high-load bearings in SAG mill gearboxes?
Use synthetic ISO VG 320 or 460 extreme-pressure gear oils with anti-wear additives. Maintain strict oil cleanliness (ISO 4406 16/14/11 or better) with offline filtration systems. Monitor oil temperature and conduct quarterly oil analysis for viscosity, water content, and particle counts. Partner with brands like SKF or Timken for bearing-specific greasing schedules.
How is slurry density controlled in flotation circuits to optimize recovery?
Use nuclear density gauges for real-time measurement (target 30-45% solids by weight). Automate control with PID loops adjusting thickener underflow or fresh water addition. For pyrrhotite-rich ores, consider de-sliming cyclones. Precise density ensures optimal reagent efficiency and bubble-particle attachment kinetics in rougher and cleaner cells.
What is the protocol for adjusting hydraulic pressure in cone crushers for different ore types?
Refer to manufacturer's chamber pressure charts. For hard, abrasive ore, increase hydraulic pressure (e.g., to 4-5 MPa) to maintain crushing force without exceeding the relief valve setting. For sticky ore, slightly reduce pressure to aid clearing. Always verify tramp release system functionality weekly to protect the main shaft and head from overload.