| Low-Alumina Inert Ceramic Ball | 17–25% Al₂O₃ | 1,350–1,550 kg/m³ | Usually ≤10% | Approximately 400–1,200 N/piece, depending on diameter | Generally suitable for moderate-temperature service up to approximately 1,100°C, subject to the supplier’s test data | Support layers, liquid distribution, gas treatment, and general packed-bed applications | Confirm chemical composition, open porosity, dimensional tolerance, and batch crush-strength test results |
| Medium-Alumina Ceramic Ball | 40–60% Al₂O₃ | 1,600–2,000 kg/m³ | Usually ≤5% | Approximately 800–2,500 N/piece, depending on diameter | Commonly selected for moderate-to-high thermal and mechanical loading | Inert bed support, reactors, dryers, absorbers, and packed towers | Request bulk-density measurement method, water-absorption test method, and abrasion-loss data |
| High-Alumina Inert Ceramic Ball | 75–95% Al₂O₃ | 2,500–3,300 kg/m³ | Usually ≤3% | Approximately 1,500–5,000 N/piece, depending on diameter | Suitable for high mechanical load and elevated-temperature service, often above 1,200°C | High-temperature reactors, catalyst support beds, furnace systems, and aggressive process environments | Verify alumina phase, apparent porosity, thermal expansion, thermal-shock resistance, and crushing strength |
| Dense Alumina Ball | 95–99% Al₂O₃ | 3,500–3,800 kg/m³ | Typically ≤1% | Approximately 2,500–8,000 N/piece, depending on diameter | Designed for severe wear, high temperature, and chemically demanding conditions | Grinding media, high-wear process zones, specialty reactors, and precision ceramic applications | Check purity, density, hardness, wear rate, surface finish, and lot-to-lot dimensional consistency |
| Ceramic Support Ball | Typically 17–75% Al₂O₃ | 1,350–2,700 kg/m³ | Typically 1–10% | Must be selected according to bed load and ball diameter | Used beneath catalyst or packing layers; operating temperature depends on composition | Catalyst-bed support, load distribution, prevention of fine-particle migration, and void-volume control | Confirm spherical geometry, size distribution, static load capacity, chemical inertness, and fines generation |
| Small-Diameter Ceramic Filler Ball | Composition-dependent | Approximately 1,400–3,500 kg/m³ | Composition-dependent | Lower force per piece; bed-load calculation is essential | Selected where higher contact area and reduced void size are required | Liquid distribution, packed columns, filtration layers, and laboratory-scale reactors | Evaluate particle-size tolerance, pressure drop, packing density, and risk of flow restriction |
| Large-Diameter Ceramic Filler Ball | Composition-dependent | Approximately 1,400–3,500 kg/m³ | Composition-dependent | Higher individual load capacity; verify with the actual diameter | Selected for lower pressure drop, robust support, and deep packed beds | Large reactors, tower support layers, high-flow systems, and industrial gas-treatment units | Check diameter tolerance, roundness, packed-bed void fraction, impact resistance, and handling losses |