Engineered Grinding Media · Mill OptimizationChina · Central Asia · Global Support
APPLICATION CASE

Customer Case Study of 120 mm Forged Grinding Balls at a Large Gold Mine

Two-stage closed-circuit grinding system (1# SAG Φ10.40×6.10m + 2# Φ8.20×14.00m). From June 2026, customized Goldpro 120 mm forged steel balls were used to phase out competitor EVRAZ balls in stages. Unit consumption for 1# dropped by 31% and for 2# by 30%, while mill throughput efficiency and grinding fineness remained stable.

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Ore typeGold Ore
Grinding stageTwo-Stage, Closed-Circuit Grinding: No. 1 SAG Mill (Φ10.40 × 6.10 m) + No. 2 Ball Mill (Φ8.20 × 14.00 m); No. 1 mill charged with Goldpro 120 mm forged grinding balls.
Primary objectivesReduce specific steel ball consumption and media procurement costs · Stabilize grinding fineness and classification, ensuring flotation dissociation · Reduce manual replenishment operation workload.
Validation methodTwo-Stage Quantified Ball Addition and Comparative Trial (replacement and testing phases), with continuous monitoring via the mine's automated control system (SCADA) of throughput, power consumption, mill filling rate, grind fineness, and full-size-range particle size distribution.
CHALLENGE

High competitor-ball consumption, fluctuating grind fineness, and frequent manual ball replenishment led to both high consumables costs and heavy on-site maintenance workload.

Mill No. 1: Baseline ball consumption of 0.41 kg/t, fluctuating grind fineness, unstable classification, and extensive manual ball replenishment.

①High grinding ball consumption: Mill No. 1 had a baseline specific consumption of 0.41 kg/t, driving up consumables procurement costs.
②Fluctuating grind fineness and unstable classification compromised mineral liberation and flotation performance.
③Frequent, high-volume manual ball replenishment increased on-site maintenance workload.

SOLUTION

We achieve optimization through these methods

Size-Specific Customized Grinding Media Matching+Four-stage Controlled Industrial Testing+Continuous SCADA Data Monitoring

①Coarse Grinding: No. 1 mill charged with customized 120 mm Goldpro forged grinding balls.
②Four-Stage Trial: Establish baseline performance →Adjust ball charge to operating conditions → Stabilize operation and collect data → Evaluate results and issue report.
③Continuous SCADA Monitoring: Track discharge particle size distribution, throughput, discharge density, circulating load, power consumption, ball charge, broken ball quantity, mill filling rate, liner condition, screen blockage rate, and full-size-range particle size distribution. Photograph and retain records of broken balls.

IMPLEMENTATION

Since June 2026, a two-phase trial involving gradual replacement and testing with controlled ball additions has been conducted to determine the optimal ball charging regime.

Continuous monitoring and comparative analysis based on data from the site’s automated control system.

  1. Establish Baseline Performance and Optimize Operating ConditionsPhase 1: Record baseline mill performance. Phase 2: Adjust the grinding ball charge and optimize the mill to its target operating conditions.
  2. Stable Operation and Data CollectionPhase 3: Once stable operation is achieved, continuously collect data on throughput, power consumption, mill filling level, discharge particle size distribution, and full-size-range particle size distribution.
  3. Results Evaluation and Standardization of the Ball Charging RegimePhase 4: Evaluate trial results, prepare the trial report, and standardize the optimal ball charging and replenishment regime.
MEASURED RESULT

Four Key Risks Mitigated Simultaneously

High Consumables Cost RiskSignificantly reduced grinding ball consumption, lowering procurement costs over the long term.
Operating Condition Fluctuation RiskStandardized, quantified ball replenishment maintains stable mill filling rate and power draw over the long term, ensuring consistent grind size.
Risk of Failing to Meet Process SpecificationsFull-process fineness control ensured balanced comminution (crushing/grinding) across both stages, securing feed quality for flotation.
On-Site Maintenance Workload RiskReduced the frequency of ball replenishment, lowering manual workload and labor intensity.