processconvert
Comminution

Grinding Circuit Calculations Explained

The concept anchor for comminution calculations — circulating load, screen (undersize-recovery) efficiency, reduction ratio, and Bond Work Index, all from measured operating data. Carries the operating-checks-vs-design boundary: these check and estimate; they do not size equipment, predict grindability, or simulate a circuit.

TypeEngineering guide — concept explainer

Definition

Grinding circuit calculations are the preliminary, formula-based checks a mineral-processing engineer uses to turn measured operating data into circuit metrics: the circulating load of a closed grinding circuit (the recycle tonnage relative to fresh feed), the screen efficiency or undersize recovery of a classifying screen, the comminution reduction ratio (how much coarser the feed is than the product), and the Bond specific grinding energy or operating work index. Each one is an accounting or textbook-equation calculation on numbers you already have — tonnages, undersize masses, F80/P80 sizes, or a supplied work index. None of them designs equipment, predicts how an ore will grind, or simulates a circuit. They are the everyday arithmetic of running and understanding a grinding circuit, scoped strictly to checks, teaching, and early-stage screening.

Why it matters

The sharpest line in this whole topic is operating checks versus design and prediction. Circulating load tells you the recycle tonnage relative to fresh feed — it is not cyclone classification efficiency, mill power, or grinding efficiency. Screen efficiency here is specifically undersize recovery (the fraction of true undersize in the feed that actually reports to the undersize product) — it is not a screen sizing or deck-selection method, and it says nothing about aperture, blinding, moisture, or capacity. Reduction ratio is same-unit sizing arithmetic, F80/P80 — it is not equipment selection and carries no energy, work index, throughput, or capacity information. Bond Work Index calculation applies a published energy equation to a work index you supply — it is not a Bond grindability test and does not determine your ore's work index. Confusing any of these for the design or prediction version is the classic error: a circulating-load number does not size a cyclone, a reduction ratio does not pick a crusher, and a Bond energy estimate does not size a mill. Getting the boundary right is what keeps these calculations honest and useful.

Formula

Circulating load ratio
CLR = recycle / fresh feed
Circulating load percent
CL% = CLR × 100
Total mill feed
fresh feed + recycle
Screen efficiency (undersize recovery)
E% = undersize product / undersize in feed × 100
Reduction ratio
R = F80 / P80
Bond specific energy
W = 10 · Wi · (1/√P80 − 1/√F80)

Units involved

  • fresh feed, recycle, total mill feed — tonnage rates (t/h)
  • undersize in feed, undersize product — tonnage rates (t/h)
  • CLR — circulating load ratio, dimensionless (×100 for %)
  • E — screen efficiency / undersize recovery, %
  • F80, P80 — 80% passing sizes in the same unit (µm or mm); reduction ratio is dimensionless
  • Wi, W — Bond work index and specific grinding energy (kWh/t), with F80/P80 in micrometres (µm)

Concept diagram

Grinding circuit calculations — operating checks from measured data, not designfresh feedmillclassifierproductcirculating load (recycle)circulating load · screen efficiency · reduction ratio · Wiall from measured operating dataoperating checks & textbook estimates — not design, sizing, or simulation

Worked example

A closed circuit runs 100 t/h fresh feed with 250 t/h recycle; a screen carries 80 t/h undersize in its feed and 68 t/h passes; the mill reduces F80 2000 µm to P80 106 µm. Compute the core circuit metrics.

  1. 01Circulating load ratio: CLR = 250 / 100 = 2.5 → 250%
  2. 02Total mill feed: 100 + 250 = 350 t/h
  3. 03Screen efficiency: E = 68 / 80 × 100 = 85.0%, with 12 t/h undersize lost to oversize
  4. 04Reduction ratio: R = 2000 / 106 = 18.87, a 94.7% size reduction
  5. 05Read all four as operating checks for the sampled period — not a sizing or performance prediction
Result

CLR 2.5 (250%), total mill feed 350 t/h, screen efficiency 85.0%, reduction ratio 18.87 — preliminary operating checks from measured data.

Common mistakes

  • Treating circulating load as cyclone classification efficiency — it is a recycle mass-flow ratio, not a partition curve.
  • Reading screen efficiency as a screen sizing or capacity result — it is undersize recovery only.
  • Mixing units between F80 and P80 in the reduction ratio — both must be in the same unit.
  • Using the Bond energy estimate to size or select a mill, or treating it as a grindability test.
  • Assuming any of these predicts how a specific ore will grind or how a circuit will perform.
  • Trusting the metrics when the input tonnages or sizes are not representative or reconciled.

When to use the calculator

Use the circulating load calculator for the recycle ratio and total mill feed of a closed circuit. Use the screen efficiency calculator for undersize recovery across a classifying screen. Use the reduction ratio calculator for F80/P80 and percent size reduction in the same unit. Use the Bond work index calculator for specific grinding energy from a supplied work index, or the reverse operating work index from measured energy. All four are preliminary checks — for equipment sizing, ore-specific grindability, or circuit performance, use testwork, vendor methods, and qualified review.

FAQ

Is circulating load the same as cyclone (classification) efficiency?
No. Circulating load is the recycle tonnage relative to fresh feed (CLR = recycle / fresh feed). Cyclone or classification efficiency describes how sharply the classifier splits coarse from fine — a partition curve with a cut size and bypass. They are related in a circuit but they are different numbers, and this calculator computes only the circulating load mass-flow ratio.
What does screen efficiency mean here?
It is undersize recovery: the fraction of the true undersize in the feed that actually reports to the undersize product, E% = undersize product / undersize in feed × 100. It is not a full screening model, a screen sizing method, or a deck-selection tool, and it does not account for aperture shape, blinding, moisture, near-size particles, or capacity.
Does reduction ratio tell me which crusher or mill to use?
No. Reduction ratio is F80/P80 — same-unit sizing arithmetic that quantifies how much size reduction occurred. It carries no energy, work index, throughput, or capacity information, so it cannot select or size equipment. Equipment selection needs testwork, vendor data, and qualified review.
Is the Bond Work Index calculation a grindability test?
No. The Bond calculator applies the published Bond Third-Theory energy equation to a work index you supply, or back-calculates an operating work index from measured energy. It does not perform the Bond locked-cycle grindability test, does not determine your ore’s work index, and does not size a mill. See the Bond Work Index Explained guide for the boundary in depth.
Can I use these calculations for design?
No. They are preliminary operating checks and textbook estimates for understanding, teaching, and early screening. Equipment sizing, vendor selection, plant optimisation, circuit simulation, and ore-specific performance prediction are out of scope and require measured plant data, testwork, vendor methods, and qualified engineering review.

Related calculators

Related conversions

Related guides