- Technical Analysis of Sluice Setup Factors in Gold Recovery
- Proper Slope (Inclination Angle)
- Sluice Width (Not Length)
- Sluice Length (Determined by Capture Media, Not Flow Alone)
- Water Flow Rate (Discharge Volume and Velocity)
- Feed Rate (Material Input per Unit Time)
- Feed Material Consistency (Particle Size Distribution and Moisture Content)
- Sluice Box Design (Riffles, Matting, and Traps)
- Location & Placement of Sluice (Site Stability and Hydrology)
- Particle Sizes (Must Be Known Before Rigging)
- Particle Shapes (Corey Shape Factor)
- Feeder Configuration (Feed Management)
Technical Analysis of Sluice Setup Factors in Gold Recovery
Below is a technical and scientifically reasoned expansion of the major factors in a sluice setup, based on Start Your Own Gold Mine guidance and aligned with best practices in gravity separation for small- to large-scale gold recovery. This analysis integrates fluid dynamics, particle behavior, and engineering principles to explain why each factor is critical to optimal gold retention and overall sluice efficiency.
A sluice box is a gravity-based concentration device used to separate gold from alluvial or placer material by exploiting differences in specific gravity (density) between gold (~19.3 g/cm³) and gangue minerals (typically 2.5–3.0 g/cm³). The effectiveness of a sluice depends not on a single variable but on the interdependent optimization of multiple physical and operational parameters. Improper configuration can result in gold loss, especially fine or flour gold, due to inadequate settling,turbulence, or washout.
Below are the nine critical technical factors governing sluice performance, with in-depth explanations of their roles and underlying principles.
Proper Slope (Inclination Angle)
Technical Role:
The slope of the sluice box governs the velocity of water flow , which critically determines whether the flow remains laminar or transitions to turbulent, and directly affects particle settling dynamics and bed load transport efficiency. This balance is essential for effective gravity separation of high-density minerals like gold from lighter waste material.
Scientific Rationale:
The optimal inclination angle for most sluice operations falls within the range of 1° to 15° (approximately 1–2 inches of drop per foot of length), with exact values dependent on feed particle size, slurry density, and available water volume.
At slopes below 1°, water velocity becomes too low to maintain adequate transport of lighter matrix materials (such as sand and gravel), leading to material buildup, clogging, and reduced operational throughput.
Conversely, slopes exceeding 4° generate excessive flow velocities, promoting turbulent flow conditions that increase fluid energy. This turbulence suspends fine, high-density particles—like gold flakes—preventing them from settling into the riffles where they would otherwise be captured.
Stokes’ Law provides a foundational explanation: the settling velocity of a spherical particle in a fluid is proportional to the square of its diameter and the density difference between the particle and the fluid. When water velocity exceeds the terminal settling velocity of fine gold particles (often <150 microns), these particles remain entrained in the flow and are lost downstream—a phenomenon known as washout.
To achieve efficient separation, the slope must be carefully calibrated in conjunction with water discharge rate and riffle geometry to maintain critical bed shear stress. This ensures that the flow is energetic enough to erode and remove lighter materials (competent bed load transport), yet gentle enough to allow gold to drop out of suspension and be trapped within the sluice’s retention zones.
Conclusion: The slope of the sluice is a precisely tuned parameter, not a matter of convenience or tradition. It must be optimized to establish critical flow conditions—where hydraulic forces selectively transport waste material while enabling gold to settle and be retained, maximizing recovery efficiency.
Sluice Width (Not Length)
Technical Role:
The width of a sluice governs the cross-sectional area available for flow distribution, directly impacting flow uniformity, bed shear stress, and ultimately, gold capture efficiency. Unlike length, which primarily affects residence time under specific conditions, width plays a foundational role in how slurry is spread across the sluice matrix, influencing the hydrodynamic environment where particle settling and retention occur.
Scientific Rationale:
Increasing sluice length without corresponding adjustments to slope, flow rate, or riffle design often results in flow stagnation at the downstream end. This reduces bed shear and flow energy to suboptimal levels, impairing the ability to flush lighter material while failing to enhance fine gold retention—leading to diminished recovery.
In contrast, increasing sluice width expands the effective settling and retention area, enabling higher feed volumes without a proportional increase in flow velocity. This maintains favorable flow conditions (e.g., laminar to transitional flow) that support particle stratification and gold settling.
Wider sluices (e.g., 12–18 inches) facilitate lateral dispersion of slurry, promoting even flow distribution and minimizing high-velocity channels or localized turbulence. This enhances the formation of consistent eddy currents behind riffles, improving the capture and retention of heavy minerals like gold.
However, excessive width (typically >24 inches) without sufficient water volume and feed distribution mechanisms can create peripheral dead zones. These low-energy regions along the sidewalls encourage eddy formation that traps and then releases fine gold during flow fluctuations, resulting in losses.
Maintaining a subcritical Froude number (Fr = v/√(g·h), where Fr < 1) is essential for stable flow. Wider sluices, when properly fed, help sustain subcritical conditions by limiting flow depth increases and preventing hydraulic jumps that disrupt particle settling and bed layer formation.
Conclusion: Sluice width significantly enhances recovery performance by optimizing flow distribution, increasing effective processing area, and stabilizing hydraulics for gold stratification and retention. In contrast, increasing length alone provides minimal benefit—and can be detrimental—unless accompanied by recalibration of slope, riffle configuration, and flow dynamics. Therefore, width is the more critical dimension for maximizing efficiency in sluice design.
Sluice Length (Determined by Capture Media, Not Flow Alone)
Technical Role:
The length of a sluice is not an independent design variable for enhancing recovery, but rather a derived outcome of the required retention zone for specialized capture materials—such as riffles, matting systems (e.g., Cleangold, Miner’s Moss), and nugget traps—engineered to retain fine gold at a given capacity. Length must be calibrated to ensure complete utilization of the capture media’s retention potential, not to artificially extend residence time under poorly controlled hydraulics.
Scientific Rationale:
Sluice length should be determined based on the proven performance length of the installed recovery system. For example, scientific testing and field validation show that a Cleangold matting system requires approximately 180 cm (6 feet) of effective contact length to achieve optimal fine gold recovery at a feed rate of 3 tonnes per hour. This length ensures that turbulent boundary layer interactions and micro-eddy retention mechanisms function as designed.
Beyond this optimal length, additional sluice extension offers diminishing returns and may lead to flow separation, reduced shear stress, and sludge buildup, especially if slope and flow velocity are not re-tuned. The downstream portion of overlong sluices often becomes a low-energy tail zone where fine gold can be washed out during surges or lost in stagnant deposits.
Laminar flow cannot be achieved solely by increasing length. Despite common misconceptions, water flow in sluices is inherently turbulent due to slurry introduction, particle collisions, and surface roughness. True flow stabilization depends on width-to-flow ratio, uniform feed distribution, and bed texture, not extended length. In fact, longer sluices without proportional width increase tend to develop velocity gradients across the cross-section, undermining uniform particle settling.
The primary hydraulic control for laminar-like behavior is width, which allows for lower flow velocities at high throughput by increasing cross-sectional area. A wider sluice with adequate feed spread maintains transitional to mildly turbulent flow, ideal for gold settling into interstices of matting and riffles—whereas excessive length without width leads to decelerated, non-uniform flow that disrupts bed dynamics.
Design rigging during sluice engineering involves matching feed rate, water volume, slope, width, and capture media type to determine the minimum effective length needed for full engagement of the retention system. For instance:
- At 3 t/h, 180 cm of Cleangold matting provides >95% fine gold recovery.
- At 6 t/h, either doubling width or using two parallel 180 cm lanes is preferable to extending a single lane to 360 cm, which risks flow stratification and edge losses.
Recovery efficiency is maximized when length matches the saturation point of the capture medium—i.e., the distance over which >90% of target particles are entrained. Beyond this, mechanical cleaning cycles, flow surges, and bed compaction increase the risk of carpet blowout or fine gold scouring.
Conclusion: Sluice length is a consequence of capture media requirements, not a primary lever for recovery improvement. Optimal length is rigorously defined by experimental data on matting and riffle performance at specific capacities. Instead of extending length, focus should be placed on sufficient width, uniform slurry distribution, and proper hydraulic balance to maintain effective flow conditions across the entire width and length of the system. Width governs flow dynamics; length serves retention mechanics.
Water Flow Rate (Discharge Volume and Velocity)
Technical Role:
Regulates transport energy, bedload mobility, and separation efficiency within the flowing water matrix. It is a key determinant of how effectively material is processed and how well high-density particles like gold are retained.
Scientific Rationale:
The water flow rate—measured in gallons per minute (GPM) or cubic meters per hour (m³/h)—must achieve a balance: sufficient to fluidize the bed and convey silts, sands, and lighter debris downstream, yet controlled enough to avoid suspending fine gold particles.
Flow dynamics are governed by the Reynolds number (Re), which characterizes the flow regime:
- Re < 2,000: Laminar flow predominates, favoring particle settling and stratification—beneficial for gold deposition behind riffles.
- 2,000 ≤ Re ≤ 4,000: Transitional flow, less predictable and potentially disruptive.
- Re > 4,000: Turbulent flow increases particle suspension, raising the risk of fine gold being washed out of the sluice.
For a standard 12-inch wide sluice, optimal performance is typically observed at 50–100 GPM, depending on slope, material load, and riffle design.
Excessive flow elevates bed shear stress, which can dislodge gold trapped in riffles or matting, especially if the sluice lacks proper turbulence-dampening features.
Insufficient flow leads to sediment accumulation, clogging riffles and reducing trapping efficiency. This results in physical burial of gold beneath non-moving material, increasing the likelihood of loss during cleanup.
Conclusion: Flow rate must be precisely calibrated to maintain a critical suspension threshold—adequate to transport waste material and prevent clogging, but low enough to ensure that gold, particularly fine or flake-sized particles, settles into and remains trapped within the recovery system.
Feed Rate (Material Input per Unit Time)
Technical Role:
Controls the material loading density on the sluice bed, directly influencing bed stratification dynamics and riffle efficiency in capturing high-density particles like gold.
Scientific Rationale:
- An excessive feed rate exceeds the sluice’s separation capacity, resulting in:
- Riffle burial, where incoming material blankets the riffles, trapping gold before it can settle into retention zones
- Reduced particle settling time, limiting the ability of dense particles to migrate downward through the flow layer
- Increased turbulence and inter-particle interference, as overcrowding promotes collisions that disrupt laminar flow and hinder size/weight-based sorting
- An optimal feed rate promotes thin, continuous material deposition, facilitating:
- Effective size and density stratification within the moving bed
- Unimpeded percolation of gold particles through the lighter matrix into riffle traps and matting
- Feed rate must be balanced with water velocity and sluice cross-sectional area to maintain a critical solids concentration—typically <30% by volume—to ensure fluidized bed behavior without slurry congestion
- Mismatched high feed rates elevate mechanical entrainment losses, particularly for fine gold (<100 mesh), which lacks sufficient mass to settle rapidly under turbulent conditions
Conclusion: Feed rate must be precisely synchronized with hydraulic capacity to avoid bed overloading, sustain efficient gravity separation, and maximize recovery across all particle sizes.
Feed Material Consistency (Particle Size Distribution and Moisture Content)
Technical Role:
Enables efficient hydraulic stratification within the sluice by promoting uniform layering of material, while minimizing operational disruptions such as segregation, clogging, or channeling across the riffle system.
Scientific Rationale:
- Variable particle sizes (e.g., unprocessed mixtures of boulders, sands, silts, and clays) disrupt flow dynamics and settling behavior:
- Bridging occurs when oversized particles (e.g., gravel or cobbles) obstruct water flow and trap finer material, reducing access to the concentrating surface.
- Clay balling is prevalent in high-moisture, clay-laden feeds, where agglomerates form and encapsulate gold particles, preventing their settlement into traps.
- Segregation happens when coarse particles migrate differently than fines—often rolling over riffles and creating turbulence that washes away fine gold.
- A uniform particle size, typically achieved by screening feed to <3/8 inch (10 mm), ensures more consistent settling velocities (per Stokes’ Law), allowing gold to stratify effectively and settle behind riffles.
- Moisture content significantly influences feed rheology:
- Excessive moisture promotes cohesion in clays, reducing particle dispersion and hindering liberation.
- Dry, dusty material may fluidize excessively, reducing bed stability and trapping efficiency.
- Optimal moisture supports a homogeneous slurry that flows steadily without agglomeration or turbulence.
- Pre-treatment requirements:
- Clay-rich or high-moisture feeds demand pre-washing or mechanical scrubbing to break down aggregates and liberate occluded gold.
- Understanding liberation size is critical—gold encapsulated in sulfide minerals or coarse quartz veins may not be gravity-recoverable without prior crushing or grinding.
Conclusion: Consistent, pre-processed feed—controlled for both particle size distribution and moisture content—is essential for maximizing hydraulic sorting efficiency, enhancing gold retention, and minimizing mechanical and fluid dynamic losses in sluice operations.
Sluice Box Design (Riffles, Matting, and Traps)
Technical Role:
Generates low-pressure zones and dampens turbulence to effectively capture and retain gold particles during slurry flow.
Scientific Rationale:
- Riffle design (governing height, shape, and spacing) directly influences eddy formation downstream of obstructions, creating zones of recirculating flow where gold can settle.
- Taller riffles (>1 inch) are effective at trapping coarse gold but may cause overloading or burial of fine particles under high flow rates.
- Shorter, closely spaced riffles—such as Hungarian, ripple, or super sluice patterns—enhance turbulence modulation and improve retention of fine and flour gold by maintaining consistent low-velocity pockets.
- Matting materials (e.g., miner’s moss, ribbed rubber, astroturf, or carpet) function as a secondary capture mechanism, exploiting boundary layer dynamics near the sluice bed. These materials reduce flow velocity at the substrate level, allowing ultra-fine gold (<100 mesh) to settle and adhere through laminar sublayer trapping and mechanical entrapment.
- Internal trapping systems—including expanded metal grates, classifier plates, and vortex traps—engineer low-velocity or stagnant zones within the flow path, promoting sediment stratification and enabling dense gold particles to drop out of suspension while lighter material continues downstream.
- Laminar flow promoters, such as flow splitters, baffles, or tapered sidewalls, mitigate velocity differentials between the center and edges of the sluice, ensuring more uniform flow distribution and reducing short-circuiting that can flush fine gold downstream.
Conclusion: Optimal sluice box performance hinges on precise control of flow turbulence and maximization of boundary layer retention, with particular emphasis on capturing sub-100 mesh gold particles through integrated riffle geometry, matting, and engineered traps.
Location & Placement of Sluice (Site Stability and Hydrology)
Technical Role:
Ensures operational continuity, safety, and environmental compliance by integrating the sluice into a site that supports efficient, sustainable, and lawful gold recovery.
Scientific Rationale:
- Stable foundation is essential to maintain sluice alignment and integrity—vibrations or ground shifting can disrupt the riffle matrix, reducing gold retention and increasing the risk of fine gold being washed out.
- Proximity to water source directly impacts energy efficiency; closer access reduces reliance on mechanical pumping, lowering fuel or electricity costs and minimizing equipment wear.
- Terrain gradient influences hydraulic performance—optimal slope ensures proper water velocity for gold settling without causing turbulence that could lead to gold loss. Excessive gradients may require flow regulation through weirs, check dams, or settling ponds to stabilize delivery.
- Environmental impact mitigation is both an ethical and regulatory imperative:
- Sediment runoff must be controlled using settling ponds or sediment traps to prevent downstream siltation, which harms aquatic ecosystems and violates water quality standards.
- Riparian zone protection requires adherence to buffer zone regulations to preserve vegetation, prevent erosion, and maintain habitat integrity.
- Accessibility ensures that maintenance, cleaning, and concentrate removal can be performed regularly and efficiently—remote or poorly accessed sites increase downtime and labor costs, reducing overall productivity.
Conclusion: Poor placement leads to mechanical failure, environmental penalties, and lost production—underscoring the need for a scientifically informed, regulation-compliant site selection process.
Particle Sizes (Must Be Known Before Rigging)
Technical Role:
Understanding the particle size distribution of gold in the ore body is a critical prerequisite before setting up or rigging any gold recovery system. This knowledge directly influences:
The design and configuration of sluices, including riffle type, spacing, and depth
The necessity and setup of pre-screening or classification systems (e.g., trommels, screens, cyclones)
The expected recovery efficiency across different size fractions—especially fine gold (flour gold) versus coarse nuggets
Selection of appropriate sluice variants.
Without accurate particle size data, recovery systems risk being improperly configured—leading to gold loss, inefficient processing, or equipment overload.
Scientific Rationale:
Gold does not occur uniformly in nature; it exists in a range of particle sizes—from visible nuggets to sub-micron “invisible gold.” The physical behavior of gold particles during processing is heavily dependent on their size and mass. Therefore, characterizing particle size distribution is grounded in fundamental principles of mineral processing physics and fluid dynamics.
Key scientific considerations include:
Settling Velocity (Stokes’ Law & Hindered Settling):
- Larger, heavier particles settle faster in water than fine particles.
- Fine gold behaves unpredictably in flowing water due to turbulence and can be easily washed out of poorly designed sluices.
- Knowing the size distribution allows for optimizing water velocity and flow depth to ensure gold settles into traps while waste material (gangue) is carried away.
Riffle Design and Sluice Hydraulics:
- Coarse gold requires deeper riffles with wider spacing to prevent bounce-over and allow trapping.
- Fine gold demands tighter riffle spacing, carpet-like matting (e.g., ribbed rubber matting), or specialized traps (e.g., vortex traps) to enhance retention.
- Mismatched riffle design leads to inefficient gold capture—either by allowing fine gold to escape or by clogging with oversized material.
Need for Classification:
- If feed material contains a wide range of particle sizes, pre-screening is essential.
- Undersized material (fines) can be processed through high-efficiency fine-gold recovery circuits (e.g., centrifugal concentrators).
- Oversized material (gravel, rocks) must be removed to prevent sluice clogging and reduced bed mobility, which hampers gold stratification.
Downstream Processing Efficiency:
- Particle size affects not only gravity methods but also alternative techniques like flotation or leaching (though leaching is avoided in this program).
- Even in mercury-free and cyanide-free systems, liberation size—the point at which gold is freed from host rock during crushing—is crucial.
- Inadequate grinding may leave gold locked in larger particles, resulting in poor recovery yields.
Empirical Validation:
- Field studies and metallurgical testing show that operations that characterize feed particle size before rigging achieve 20–40% higher recovery rates than those that do not.
- For example, a site with predominantly fine gold may require a multi-stage recovery system, whereas coarse gold may be efficiently captured in a well-riffled sluice alone.
✅ Bottom Line: You cannot recover what you don’t understand.
Knowing gold particle sizes before rigging transforms gold recovery from guesswork into a predictable, scientific, and profitable process. It is not just a technical detail—it is the foundation of efficient, sustainable, and high-yield gold mining.
Particle Shapes (Corey Shape Factor)
Technical Role
- Shape tells us how gold will behave in moving water.
- The Corey shape factor (φ = d₍max₎ / d₍min₎) gives a quick, practical cue for tailoring riffle spacing, matting depth, and flow‑rate to the real‑world geometry of the ore.
- High‑φ (flat/elongated) particles need tighter riffles, thicker matting, and slower flow to stay in the sluice, while low‑φ (round) particles can be handled with standard riffles and a higher flow rate.
Scientific Rationale
- Drag & Lift: Flat or elongated particles present a larger surface to the water, increasing drag and generating lift that keeps them in suspension.
- Settling Velocity: For the same density, a higher φ means a slower terminal settling speed, raising the chance of wash‑out.
- Bed Interaction: Angular or elongated particles can bridge or channel the flow, reducing effective shear and letting fine gold slip downstream.
- Retention Zones: Riffles create eddies and low‑velocity pockets; their size must match the particle shape to trap gold effectively.
Bottom Line
Knowing the Corey shape factor lets you match the sluice design—riffle spacing, matting, flow—to the actual particle shapes in your feed, keeping more gold in the box and cutting loss from wash‑out.
Feeder Configuration (Feed Management)
Technical Role
The feeder is the first point of contact between the raw ore and the sluice.
It determines how much material, how fast, and with what characteristics (size, moisture, shape) reach the sluice entrance. By controlling:
- Feed rate (tons per hour or volume per minute)
- Particle size distribution (via pre‑screening or trommels)
- Moisture & cohesion (through pre‑washing or dry‑feed systems)
- Feed uniformity & distribution (through belt‑type or chute feeders)
the feeder sets the hydraulic load and sedimentation dynamics that the sluice will experience. A well‑designed feeder keeps the sluice at its optimal operating window—maximizing gold retention, minimizing clogging, and reducing the risk of wash‑out.
Scientific Rationale
| Feed Parameter | Effect on Sluice Dynamics | Practical Implication |
|---|---|---|
| Feed Rate (Qₓ) | Determines bedload concentration; high Qₓ increases shear stress and can raise the bed‑load transport threshold. | Too high → riffle burial, loss of fine gold; too low → sluggish flow, poor gangue transport. |
| Particle Size Distribution | Influences settling velocity (Stokes’ law) and the likelihood of bridging or channeling. | A mix of coarse and fine particles creates stratification; pre‑screening removes oversized material that could clog riffles. |
| Moisture Content | Alters rheology; high moisture can cause clumping (clay balling) and increase effective density. | Dry feeds improve fluidization; wet feeds may need pre‑washing to prevent flocculation and improve liberation of gold. |
| Feed Shape & Cohesion | Flattened or elongated particles interact differently with flow, affecting lift forces and residence time. | Feeder design should promote even spread; for angular feeds, use wider belts or chutes to reduce channel formation. |
| Feed Uniformity | Non‑uniform feed creates local spikes in shear stress, leading to short‑circuiting or turbulence that washes gold. | Use belt‑type feeders with spreaders or rotary screens to distribute material evenly across the sluice width. |
Key Physical Concepts
- Critical Shear Stress (τc): The minimum bed shear required to mobilize particles of a given size and density. The feeder must deliver a feed rate that keeps the actual shear (τ) near but not exceeding τc for the target particle size.
- Bed Load Transport (Rouse Number): The ratio of settling velocity to suspension velocity. A well‑tuned feeder keeps the Rouse number high enough for gold to settle but low enough for lighter material to move downstream.
- Hydraulic Loading: Defined as (Qₓ / (width × depth)). Proper feeder loading ensures sub‑critical flow (Froude < 1) so that eddies behind riffles can form and trap gold.
Design & Operation Guidelines
Pre‑Screening
- Install a 3/8” or 1/2” trommel before the feeder to remove oversized rock that would otherwise clog the sluice.
- For fine‑gold emphasis, use a 3/16” screen to keep fines in the stream.
Feed Rate Calibration
- Start at 25–30 % of the sluice’s maximum capacity and adjust in 5 % increments while monitoring gold recovery.
- Use a flow meter or weigh‑based feed controller for precise control.
Moisture Management
- If the ore is wet, run a pre‑wash basin or dry‑feed conveyor to reduce moisture to <10 %.
- For very dry, dusty material, add a fine‑dust catcher or a small air‑lift system to keep the feed fluidized.
Flow‑Deflector Integration
-The flow‑deflector is a simple, box‑shaped insert that sits between the feeder discharge and the sluice entrance. Its primary function is to split and spread the incoming slurry, thereby reducing the local velocity and eliminating the high‑velocity jets that can scour gold from riffles or matting. By forcing the slurry to widen before it reaches the sluice, the deflector also eliminates short‑circuiting and ensures that every particle experiences the same shear stress across the entire width of the bed. In practice, a 12‑inch wide deflector with a 3‑to‑4‑inch clearance and a modest 3‑inch wall height is sufficient for most 12‑inch sluice sizes, but the dimensions can be scaled linearly with sluice width and feed rate.
- Hydraulic Benefits and Recovery Gains. When the deflector is correctly dimensioned, the Reynolds number in the sluice entrance drops from the turbulent regime (Re > 4 000) to the transitional/laminar regime (Re ≈ 1 500–2 500). This shift dramatically improves the settling of fine gold (< 150 µm) and reduces wash‑out losses by up to 20 % in field trials. Moreover, the deflector’s uniform spread mitigates the “edge‑effect” that often causes gold to be flushed out along the sluice walls. In combination with a pre‑screened, moisture‑controlled feed, the flow‑deflector essentially locks the sluice into its “sweet spot” of sub‑critical flow (Fr < 1), optimal riffle eddies, and high gold capture efficiency.
Uniform Distribution
- Use a belt feeder with a spreader plate or a chute with a “V” cross‑section to spread material evenly.
- For large‑scale operations, consider a multi‑lane feeder to keep each sluice lane at its optimum load.
Real‑Time Monitoring
- Install a simple load cell or weigh‑bridge at the feeder exit.
- Pair with a sluice‑side sensor (e.g., water level or flow meter) to maintain the desired hydraulic loading ratio.
Maintenance
- Inspect screens, belts, and chutes for wear every 50–100 t of processed ore.
- Clean the feeder bed and discharge area regularly to prevent accumulation of fines that could reduce effective feed area.
Bottom Line
A dedicated feeder section—separate from the sluice—lets you control feed rate, size, moisture, and uniformity before the material hits the sluice. By doing so, you keep the sluice operating in its sweet spot: enough energy to move waste but gentle enough to let gold settle. This upstream optimization is a proven way to boost overall recovery and keep the sluice running clean and efficient.
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