Where Our Media Works
Tell us the stream, the target spec and the operating window. We match the exact alumina or zeolite grade, pore size and shaping — then prove it with a free sample and a written test protocol.
Core Applications

Reach −40 to −70 °C pressure dew point on instrument and process air. Activated alumina for general duty, 3A/4A molecular sieve when the dew point must stay low through temperature swings.
Matching grades →
Blower-heated and heat-of-compression regeneration cycles. Our 1.6–2.5 mm spheres are dust-controlled to protect downstream valves, laser optics and pneumatic instrumentation.
Matching grades →
Polyol, refrigerant, solvent and glycol streams where 3A excludes the carrier molecule and passes only water — no product loss, no oligomer coking on regeneration.
Matching grades →
Pipeline-spec dehydration, NGL and LNG feed pretreatment, CO₂ removal. 3A for glycol-dehydrated gas, 4A/5A and 13X for acid gas and mercaptan duty.
Matching grades →
Cracked-gas and reformate drying ahead of cryogenic separation. High crush-strength 5A and 13X extrudates built for tall beds and aggressive regeneration cycling.
Matching grades →
Activated alumina media for municipal and well-water fluoride removal, arsenic co-removal and potable polishing. NSF-grade material, drum and filter media sizing support.
Matching grades →Industries We Serve








Not Sure Which Grade?
Duty conditions in, grade recommendation out — pore size, crush strength, working capacity and a regeneration window you can check against your own plant data.
Aluminaworld materials are used in eight principal industrial applications. Compressed-air drying uses 2–5 mm or 3–5 mm activated alumina balls in twin-tower heatless regenerative dryers to reach -40 °C to -50 °C pressure dew points. Natural-gas and LNG dehydration uses molecular sieve 4A and 13X beds sized by water load and cycle length. PSA oxygen and hydrogen production uses molecular sieve 5A and 13X as the adsorbent in pressure-swing adsorption units. Drinking-water defluorination uses high-porosity activated alumina, a WHO-recommended defluoridation medium. Transformer and electrical-insulation breathing uses activated alumina to hold the breather dry. Catalytic reforming and petrochemical processing uses activated-alumina and pseudo-boehmite catalyst carriers for Claus, H₂O₂ and FCC units. ZSM-5 catalysis covers catalytic cracking and methanol-to-olefins. Polymers and coatings use ATH as a flame retardant and molecular-sieve powder as a desiccant.
| Application | Recommended Product | Key Operating Parameter | Target Performance |
|---|---|---|---|
| Compressed-air drying | Activated alumina 2–5 / 3–5 mm | 180–220 °C regeneration, 4–6 h cycle | -40 to -50 °C pressure dew point |
| Natural gas / LNG dehydration | Molecular sieve 4A / 13X | 220–260 °C regeneration, 8–24 h cycle | Water ≤0.1 ppm vol, CO₂ <50 ppm |
| PSA oxygen / hydrogen | Molecular sieve 5A / 13X | 0.5–3.0 bar adsorption, 220–250 °C regeneration | O₂ 90–95%, H₂ 99.9% |
| Drinking-water defluorination | Activated alumina 1–3 / 2–5 mm | pH 5.5–6.5, NaOH regeneration | F⁻ down to <1.0 mg/L |
| Transformer breathing | Activated alumina 2–5 / 3–5 mm | Ambient breather, periodic heating | Insulation dry, low dew point |
| Claus / H₂O₂ / FCC catalysis | Catalyst carrier, pseudo-boehmite | Al₂O₃ 65–72%, BET 220–320 m²/g | Catalyst support durability, low attrition |
| MTO / catalytic cracking | ZSM-5 zeolite | SiO₂/Al₂O₃ ratio 25–1000 | Shape-selective propylene selectivity |
| LSZH cable / artificial marble | Aluminum hydroxide (ATH) | Whiteness and particle-size controlled | Non-toxic flame retardancy, low smoke |
Molecular sieve 4A is the standard choice for pipeline and LNG dehydration because its 4 Å aperture admits water while excluding hydrocarbons heavier than C3. 13X is used where the highest water capacity per unit volume is required and CO₂ pretreatment is available.
Yes for most industrial compressed-air applications. Activated alumina reaches -40 °C to -50 °C pressure dew point, tolerates oil and heavy contamination better, and costs less. Molecular sieve 13X is still required when the dew-point target is below -50 °C, when the air is very clean, or when the lowest possible unit-volume footprint matters.
Bed size is calculated from the water load (kg H₂O per hour), the required working capacity of the chosen grade, the mass-transfer-zone length, and a safety factor of 1.2 to 1.5. A full worked example for compressed air, natural gas and PSA oxygen is published on the Aluminaworld Insights page.
220 °C to 260 °C under a dry purge or swing gas, held for 4 to 6 hours to restore full working capacity. Activated alumina regenerates at a lower 180 °C to 220 °C.
Aluminaworld supplies the adsorbent media and can support skid design and bed sizing. Complete vessel and skid supply is available on request for large projects.