
In a gold adsorption circuit, carbon must move countercurrent while the much finer slurry continues through the tanks. When that separation becomes unstable, operators do not merely lose a tidy flow pattern: carbon can be misplaced, slurry transfer can slow, and the recovery circuit becomes harder to control. An interstage screen gives that handoff a defined boundary, but its value depends on how it manages carbon, slurry, abrasion, and cleaning as one continuous duty.
Carbon-in-leach and carbon-in-pulp circuits use a series of agitated tanks, yet the material streams have different jobs. Fine ore pulp carries the leached solution forward, while coarser activated carbon is retained and transferred in the opposite direction. The screen between stages has to preserve that distinction without becoming a choke point for the slurry.
This is why interstage screening is not simply a size-cut exercise. A nominal opening must retain the working carbon population while passing slurry at the needed rate, under agitation and with changing solids conditions. A screen that retains carbon but raises the liquid level, blinds early, or creates uneven flow still disrupts the circuit it was meant to protect.
A cylindrical interstage screen sits at the tank transfer point so slurry passes through its surface while activated carbon stays on the intended side. This supports the countercurrent path: pulp progresses through the tank train, and carbon transfers toward the previous adsorption stage.
A well-matched écran intermédiaire therefore gives the operator two useful controls at once. It keeps the carbon inventory where the circuit expects it and provides a known path for the slurry. The correct operating outcome is stable passage of pulp with minimal unintended carbon carryover, not an isolated claim about maximum open area.
A fully welded wedge wire cylinder uses profile wires and support rods to create continuous slots. Compared with an array of isolated holes, a continuous slot gives water and fine slurry more than one short path through the surface. Its V-shaped profile also widens behind the working face, which can make near-size material less likely to lodge deeply in the opening.
That geometry does not remove the need for inspection. Fibres, oversize carbon, scale, and sticky fines can still reduce available area. The practical advantage is keeping passageways accessible under appropriate agitation, flow, and cleaning conditions.
The useful slot decision begins with the actual carbon size distribution, not with a generic opening recommendation. Carbon attrition changes the proportion of fines over time, while ore fineness and slurry rheology influence how readily pulp passes through the screen. A suitable opening must account for the smallest carbon worth retaining and the duty that the slurry imposes on the screen face.
For a carbon retention screen, the operating review should also examine agitation, carbon transfer method, pulp density, available head, and cleaning access. These factors decide whether the chosen surface remains an efficient boundary between the two streams or becomes a restriction that operators have to work around.
The conditions below illustrate why an interstage duty should be assessed as a system rather than as a screen sheet alone:
| Observed condition | Likely screen effect | Useful first check |
| Higher carbon fines | More risk of unwanted carbon passage | Review current carbon size distribution and attrition trend |
| Reduced slurry transfer | Available area may be loading or blinding | Check debris, pulp density, and the cleaning routine |
| Uneven tank levels | Flow may be restricted or poorly distributed | Inspect screen condition and transfer hydraulics together |
| Fast surface wear | Slot shape and support structure can change over time | Compare wear location with slurry direction and agitation |
The screen assembly must suit the tank layout, transfer arrangement, and removal path. A cylindrical surface with the wrong diameter, length, mounting details, or clearances can make inspection and replacement harder than it needs to be. It can also create local flow conditions that add wear or concentrate material against a limited part of the surface.
BTOSLOT builds its interstage model as a stainless steel wedge wire cylinder for CIL and CIP tank service, with material and dimensions selected around the application. That is relevant because a tamis à coin Johnson is most useful when its slot, cylinder geometry, supports, and connections are considered together with the plant’s carbon and slurry data.
A sensible data set for the design discussion includes tank geometry, process flow, carbon size range, expected attrition, pulp density, ore abrasiveness, chemistry, transfer method, and how the screen will be cleaned or removed. These inputs help a plant distinguish a routine replacement from a geometry or operating mismatch that would repeat with the next unit.
An interstage screen keeps activated carbon and gold slurry on their intended countercurrent paths by allowing the fine pulp stream to pass while retaining the coarser adsorption media. Stable performance comes from matching the continuous slot surface to real carbon size, slurry behavior, tank hydraulics, wear exposure, and maintenance access.
The next practical step is to compare carbon carryover, slurry transfer, and surface condition with representative process data. This shows whether the priority is a different slot, cylinder arrangement, cleaning method, or upstream change.
It is a separation device used between adsorption stages in CIP or CIL circuits. It retains activated carbon or another granular adsorbent while allowing the finer slurry stream to continue through the process.
Both circuits need controlled separation of carbon and slurry, but tank layout, transfer method, chemistry, and operating conditions may differ. The assembly should be matched to the specific circuit rather than assumed interchangeable.
The carbon carries adsorbed gold and must follow its planned countercurrent route for recovery. Letting it pass with the slurry can disturb inventory control and send valuable carbon toward downstream sections where it is not intended to go.
Foreign material, fibres, scale, sticky fines, local overloading, or an unsuitable cleaning arrangement can reduce open area. A diagnosis should check the surface condition alongside changes in slurry density, carbon condition, and tank operation.