| Vibratory Screening and Size Classification |
Glass bead, mineral abrasive, aluminum oxide, garnet, steel shot |
70–90% |
0.5–2.0 kWh per metric ton |
None |
US$8–25 per metric ton |
Removes oversize particles, fines, and fractured grains; limited removal of oil or paint |
Good particle-size control; angularity and hardness are largely retained |
Low energy use and no process wastewater |
Does not adequately remove strongly bonded coatings or oily contamination |
| Air Classification with Dust Extraction |
Garnet, glass bead, mineral abrasive, aluminum oxide |
75–92% |
1.0–4.0 kWh per metric ton |
None |
US$12–35 per metric ton |
Separates fines, dust, lightweight debris, and some paint fragments |
Improves consistency and reduces dust generation during reuse |
Dry process with reduced hazardous-sludge generation |
Performance depends strongly on particle density and airflow control |
| Magnetic Separation |
Steel shot, steel grit, mixed ferrous abrasive streams |
90–99% |
0.1–0.5 kWh per metric ton |
None |
US$4–15 per metric ton |
Removes non-ferrous debris, paint chips, glass, and mineral contamination from ferrous media |
High retention of hardness and shape when followed by screening |
Very low energy demand and high recovery potential |
Not suitable for non-ferrous or mineral abrasives |
| Wet Hydrocyclone and Classification |
Garnet, mineral abrasive, glass bead, mixed fine abrasive |
80–95% |
0.2–0.8 kWh per metric ton |
0.1–0.5 m³ per metric ton |
US$18–45 per metric ton |
Efficiently removes low-density fines, salts, dust, and water-soluble residues |
Good particle-size uniformity after drying; grain shape is generally preserved |
Useful where dry separation cannot control fine contamination |
Requires water treatment, drying, and management of contaminated slurry |
| Thermal Reclamation |
Mineral abrasive and sand-like media contaminated with oil, paint, or organic residues |
85–98% |
20–60 kWh per metric ton |
None in the core process |
US$35–90 per metric ton |
Strong removal of organic coatings, oil, grease, and combustible residues |
High cleanliness and stable grain performance; excessive heat can damage some media |
Can substantially reduce virgin abrasive consumption and landfill disposal |
Highest energy demand; requires exhaust treatment and temperature control |
| Centrifugal Cleaning and Mechanical Attrition |
Steel shot, steel grit, durable mineral abrasives |
80–95% |
2–8 kWh per metric ton |
None |
US$15–40 per metric ton |
Removes loosely bonded paint, scale, dust, and friable surface residues |
Can improve surface cleanliness; excessive attrition may increase fines |
Dry operation with effective removal of weakly bonded contaminants |
May accelerate abrasive breakdown if residence time is excessive |
| Integrated Multi-Stage System: Screening + Air + Magnetic Separation |
Mixed streams containing ferrous and non-ferrous abrasive particles |
85–98% |
2–7 kWh per metric ton |
None |
US$20–55 per metric ton |
Removes size outliers, fines, dust, non-ferrous debris, and many paint fragments |
Most consistent particle-size distribution and reliable blast performance |
High recovery with no process wastewater |
Higher capital cost and more complex maintenance than single-stage systems |
| Wet Washing Followed by Mechanical Dewatering and Drying |
Mineral abrasive, garnet, glass bead, reusable blasting media with soluble contamination |
65–90% |
5–25 kWh per metric ton |
0.3–1.2 m³ per metric ton |
US$30–80 per metric ton |
Effective against soluble salts, dust, fine sludge, and water-soluble residues |
Good cleanliness after complete drying; moisture control is essential |
Can recover abrasive from heavily contaminated wet or dusty waste streams |
Water treatment and drying can dominate operating cost and emissions |