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Primary vs secondary solids control: dividing the cut by size

By Othman Soliman — Solids Control & Drilling-Waste specialist, 26+ yrs (GCC & MENA). Last reviewed .

Primary solids control is the shale shaker — the first, cheapest, full-flow removal stage that takes the coarse cut straight off the flowline. Secondary solids control is everything finer that follows: the hydrocyclones (desanders and desilters), the mud cleaner, and the decanting centrifuge, each removing a smaller particle the stage before it left behind. The system is a cascade, sorted coarse to fine.

Primary: the shale shaker

The shaker handles 100% of the flow returning from the well and is the only stage that sees the whole stream. It is mechanical, simple and the cheapest barrel of removal on the rig — every solid it takes out is a solid the finer, costlier stages downstream never have to touch. A shaker running the right API screen sets the ceiling for the entire system: if it leaks coarse solids, everything below it is overloaded.

Secondary: finer cuts, in order

Secondary equipment cleans the fraction the shaker could not. Each stage makes a finer cut than the last:

StageEquipmentRough cut pointRole
PrimaryShale shaker~74–150 µm (screen-dependent)Full-flow coarse removal
SecondaryDesander (hydrocyclone)~45–74 µmCoarse sand the shaker passed
SecondaryDesilter / mud cleaner~15–44 µmFine silt; recovers barite on weighted mud
SecondaryDecanting centrifuge~2–7 µmFinest cut; barite recovery / fines removal

Why the order is fixed

Each stage protects the one after it. The shaker keeps coarse solids off the cyclone feed pump; the desander keeps the desilter cones from plugging; the desilter or mud cleaner reduces the load on the centrifuge. Run a stage out of order — or skip one — and you push a particle load onto equipment that was never sized for it. The cut points only line up if the stream passes through them coarse to fine.

The economics: a barrel of solids removed at the shaker is the cheapest you will ever remove. Leaning on the centrifuge to clean up a leaking shaker is the most expensive way to run a solids-control system — and the most common.

The rule

Build the system from the top down. Get the shaker right first — the correct API screen, intact and properly tensioned — then let each secondary stage do the finer job it is built for. The centrifuge is the polish, not the rescue. If your fine-end equipment is always overloaded, the problem is usually upstream.

Key takeaways

Primary solids control is the shaker: full flow, coarse cut, cheapest removal. Secondary is the cyclones, mud cleaner and centrifuge, each making a finer cut in a fixed coarse-to-fine order. Every stage protects the next, and every barrel removed early saves money downstream. Fix the primary stage first; the secondary stages can only do their job if the shaker does its.

Free Field Guide (PDF)

The 10 Solids-Control Numbers Every Engineer Must Track — what to measure, the formula, the field target and the red flag. Grounded in API RP 13B-1, RP 13C, EPA 40 CFR 435 & OSPAR.

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