Purchased abrasive
Diamond particles are part of the process recipe and should not automatically be classified as waste.
Recover valuable diamond abrasive while controlling sapphire debris.
Sapphire lapping uses a controlled slurry to remove material and establish flatness before later finishing steps. The slurry may contain diamond abrasive selected for a defined particle distribution, a liquid carrier and process additives. As lapping continues, sapphire debris, fractured abrasive and other contamination enter the circulating stream.
The used slurry is therefore not simply “dirty coolant.” Some suspended solids are intentional and valuable; others are generated waste. If the plant discards the complete batch when debris reaches an unacceptable level, it loses carrier fluid and remaining usable abrasive together. If it returns the slurry without control, the changing particle population may affect removal behaviour and surface consistency.
Diamond particles are part of the process recipe and should not automatically be classified as waste.
Sapphire fines, fractured particles and external contamination accumulate during production.
Particle distribution, solids concentration, viscosity and chemistry can drift as the batch is used.
The recovery target must be written before selecting equipment. One plant may want a clarified carrier stream that can be returned after formulation checks. Another may want to concentrate solids for laboratory reclassification and possible abrasive reuse. A third may only need to reduce the debris load enough to extend a controlled slurry cycle.
Centrifugal separation responds to particle density, size, shape, fluid viscosity and residence time. Valuable diamond abrasive and sapphire debris may not form two perfectly separable populations. A system should never promise selective recovery from the material names alone. The test must show what enters each output stream and whether that result remains acceptable to the lapping recipe.
Diamond abrasive and conditioned slurry represent process cost, but the correct response is not unlimited reuse. A slurry can carry more generated sapphire debris, fractured abrasive and uncontrolled particle distribution as the cycle continues. That change may influence material removal, scratch risk, flatness or the load on downstream polishing.
Recovery must therefore balance economic value with quality control. The plant needs an acceptance rule for the recovered liquid or solid stream: particle-size distribution, solids concentration, viscosity, chemistry, removal rate or surface measurement. Without that rule, a separator may produce two streams but still fail to create a usable process result.
A representative sample should include the actual carrier, additives, abrasive grade and sapphire debris at normal operating temperature. The test changes bowl speed, feed rate or residence time in controlled steps and collects both the liquid and concentrated solids streams.
Each stream should then be analysed against the recovery objective. Visual clarity alone is not enough. The useful checks may include solids concentration, particle-size distribution, viscosity, chemistry, abrasive content and a controlled lapping trial. If the valuable and unwanted particles report to the same stream, centrifugation alone may not achieve selective recovery and should not be sold as a complete solution.
The final video should show the used sapphire lapping slurry, centrifuge feed, clarified liquid stream, concentrated solids and the sampling method. Captions should state the abrasive type, slurry condition, test temperature, model and operating point.
Recommended final asset: 45–90 seconds, 16:9. Do not label the test “diamond recovery” until analysis confirms where the usable abrasive reports.
VC-600 and VC-1500 are published equipment starting points, not guaranteed recovery recipes. VC-600 provides the highest G-force in the current VC range for a laboratory-to-single-line evaluation. VC-1500 provides higher circulation flow for several lapping machines or a larger central slurry tank after the test has confirmed acceptable separation.
| Process layout | Model | Flow rate | G-force | Solids capacity | Engineering role |
|---|---|---|---|---|---|
| Sample study, single line or difficult fine-particle evaluation | VC-600 | 60 L/min | 6,500 G | 2 L | Highest G-force starting point; actual test flow may be lower than the rated maximum. |
| Multiple machines or central slurry circulation | VC-1500 | 150 L/min | 1,860 G | 8 L | Higher circulation flow after recovery quality has been demonstrated at scale. |
Automatic discharge can collect a concentrated solids stream, but the discharge path and collection container must be designed as part of the recovery process. View the Automatic Sludge Discharge Centrifuge series.
There is no published universal recovery percentage on this page. A valid result must state the feed composition, test conditions, mass balance and quality of both output streams. Economic evaluation should include slurry purchase, current discard volume, testing and reformulation cost, waste handling, operator time and any effect on wafer quality.
Start with a baseline covering slurry consumption per batch, discard trigger, abrasive specification, removal rate, surface defects, flatness or other plant acceptance measures. After testing, compare recovered material against the same criteria. An application reference can be shared on request when the source data and permission are confirmed.
Provide the slurry recipe, diamond abrasive specification, sapphire process, temperature, batch volume, current discard rule and the output you want to recover. We will define a test plan before recommending VC-600, VC-1500 or another process route.