The basic formula (Throughput × Hours × Grade × Recovery) yields hazardous results when theoretical assumptions ignore site geology. This engineering guide details the 5 operating controls, the 4 tropical field criteria (Haut-Uélé, DRC), and the progressive exploration protocol required to secure mining cash flows.
Physical constraints directly impacting the variables (Flow × Hours × Grade × Recovery) of the production model.
| N° | Criterion & Variable | Operational Mechanism & Physical Reality | Reference Range | Model Risk / Pitfall |
|---|---|---|---|---|
| 01 |
Granulometry & Gold Liberation Liberation fraction (d80) |
Fraction of gold physically free vs. locked in quartz or sulfides. Indicative benchmark: conventional sluice mats primarily retain coarser fractions (> 150 µm), whereas centrifugal concentrators can recover down to ~25 µm under tuned conditions. Actual cutoffs and separation efficiencies must be confirmed by site metallurgical sizing tests, as they vary with particle shape, slurry density, and feed rate. |
> 150 µm (sluice, indicatif) ~25 µm (centrifuge, indicatif) |
Tailings loss risk Fine gold (< 75 µm) often yields sharply reduced recovery in simple sluices without centrifugal scavenging; requires site sizing tests. |
| 02 |
Head Grade & Mining Dilution Feed grade g_feed vs in-situ grade g₀ |
Mechanical excavation unavoidably incorporates sterile hanging wall or bedrock into mineralized ore. With mass dilution fraction D = M_waste / (M_ore + M_waste), the reconciled feed grade is g_feed = g₀ × (1 - D). If dilution is defined as ratio D_r = M_waste / M_ore, then g_feed = g₀ / (1 + D_r). |
Mass fraction D: 10% to 25% (illustrative) g_feed = g₀ × (1 - D) |
Dilution risk Omitting dilution overstates gold output in proportion to sterile entrainment. |
| 03 |
Pulp Density & Slurry Water Ratio Water-to-Solid Ratio (m³/t) |
Wash water flow rate must balance pulp solids to prevent riffle bed compaction while avoiding turbulent wash-out velocities. |
3:1 to 5:1 (m³ water / m³ solid) Sluice slope: 8% to 12% |
Hydraulic scouring Improper slurry density causes riffle blinding or scouring. |
| 04 |
Net Effective Runtime Mechanical availability × Utilization |
Operating hours must strictly count continuous plant feed time. Deduct morning plant warm-ups, trommel screen de-clogging, pump maintenance, fueling, and equatorial storm halts. |
200 h to 280 h / month (indicative) Based on 26 operating days (1 shift) |
Inflated calendar basis Calendar hours without scheduled maintenance deductions distort model output. |
| 05 |
Circuit Net Recovery Rate (R) Mass balance recovery (%) |
Ratio between fine gold physically poured and total metal contained in feed ore (Recovered / Contained). Determined through systematic mass balancing and continuous assaying of solid tailings discharge. |
65 % à 75 % (sluice seul) 85 % à 92 % (+ centrifuge) |
Theoretical overestimation Gravimetric recovery on fine saprolitic gold cannot reach 90% without secondary centrifugal concentration. |
Conditions encountered in the weathered saprolites, lateritic caps, and alluviums of the Kibalian greenstone belts.
| N° | Field Factor | Geological Reality & Operating Impact | Required Engineering Measure |
|---|---|---|---|
| A |
Clay Index & "Clay Balls" Saprolites plastiques & latérites |
In tropical saprolites, sticky kaolinitic clays do not disperse in simple water sprays. They roll inside the trommel, forming "clay balls" that trap gold grains and carry them out directly to waste tailings. |
High-torque rotary scrubber Equipped with internal lifter blades; minimum residence time > 3 minutes before sizing screen. |
| B |
Flakiness & Floating Gold Tension superficielle & lamelles |
Placer and river-terrace gold is frequently hammered into ultra-thin flat flakes. Surface tension allows dry or hydro-repellent flakes to float on top of water currents and bypass traditional sluice mats. |
Wetting agents & Centrifuges Surfactant dosing in wash water and centrifugal bowl concentrators (60G forces break surface tension). |
| C |
Overburden Strip Ratio (SR) Waste volume / Pay-gravel volume |
In tropical alluvial flats and terraces, mineralized gravel beds are capped by sterile silt and lateritic clay overburden. Stripping thickness varies significantly by terrace level (typically 2 m to 6 m on local valley sections) and must be confirmed by pit logging. |
Site stripping plan Strip ratio (e.g. 2:1 to 5:1 volumetric) must be budgeted separately from washing plant throughput cost. |
| D |
Swell Factor & In-situ Density Loose bulk density vs bank density |
Compacted in-situ gravel (bank density typically 1.8 to 2.1 t/m³) expands upon excavation. Converting bank cubic meters to dry metric tonnes requires direct site density calibration. |
Systematic bulk density assays Establish local conversion factor (bank m³ to loose m³ to dry feed tonnes). |
Gradual de-risking methodology from manual pitting to industrial bulk testing before committing heavy capital expenditure.
Systematic cross-check between geological exploration data and simulation input parameters.
| Phase | Criterion Analyzed | Verification Benchmark Required | Formula Impact |
|---|---|---|---|
| Geology | Free gold liberation | Laboratory liberation assays (target > 75–80% gravity-recoverable gold for simple alluvial circuits; refractory or occluded fractions require separate metallurgical treatment). | Caps maximum metallurgical recovery (R). |
| Excavation | Dilution control | Benchmarked selective digging procedure minimizing sterile bedrock and waste mixing; in-pit grade control reconciliation. | Direct divisor on head grade (g). |
| Washing Plant | Clay disaggregation power | Rotary scrubber residence time calibrated by washability tests (typically 2 to 4 min depending on clay plasticity); tailings inspection confirming thorough disintegration of clay balls. | Protects recovered fine gold against tailings discharge. |
| Hydraulics | Slurry pulp ratio | Slurry solids density monitored within circuit design envelope (indicative operating range 20% to 30% solids by weight depending on chute slope and grain size). | Prevents mat sanding, slurry scouring, and concentrate wash-out. |
| Operations | Effective runtime hours | Maintenance logs and weather stoppages supporting realistic effective hours (e.g. 200–260 h/month per shift schedule). | Sets realistic monthly productive hours (h). |
Enter your verified throughput, realistic productive hours, net head grade (after dilution), and tested recovery rate to calculate monthly fine gold output in kilograms and troy ounces.