JUN 5, 202661 MINS READ
Aluminium oxides granules are composed of aggregated primary particles of aluminium oxide (Al₂O₃) in various crystallographic phases, predominantly transition aluminas (γ, δ, θ) and α-alumina (corundum). The granules produced via pyrogenic synthesis exhibit primary particles with diameters of 5–50 nm, which aggregate into secondary structures with mean diameters of 5–150 μm 36. The BET-specific surface area typically ranges from 20 to 200 m²/g, with higher values associated with transition aluminas and lower values with α-alumina 1013. The ratio of Sears number to BET surface area, a critical parameter for dispersion stability, falls between 0.150 and 0.160 for optimized pyrogenic alumina 1718.
The granules' structural integrity depends on the degree of primary particle aggregation and the presence of surface hydroxyl groups. Pyrogenically produced aluminium oxide granules contain aggregated primary particles with spherical morphology and absence of internal porosity, distinguishing them from sol-gel or precipitated variants 36. The tamped density, a key indicator of packing efficiency, ranges from 300 to 1200 g/l for spray-dried granules 367 and can reach 210–2000 g/l for compacted and crushed granules 48. The relative density of the aluminium oxide phase itself approximates 3.2 g/ml 20.
Phase composition critically influences mechanical and thermal properties. Transition aluminas, formed at lower calcination temperatures (350–800°C), exhibit higher surface areas and reactivity, making them suitable for catalytic applications 210. Conversion to α-alumina occurs at temperatures above 1000°C, yielding granules with enhanced thermal stability and hardness but reduced surface area 10. The α-conversion rate, defined as the mass fraction of α-alumina, can be controlled between 5% and 70% to balance reactivity and stability 71112.
Surface modification through silanization introduces organic functional groups (e.g., octyl, aminopropyl, methacryloxypropyl) that alter hydrophobicity and dispersibility. Silanized granules exhibit carbon contents of 0.3–12.0 wt%, with corresponding changes in surface energy and compatibility with organic matrices 367. The pH of aqueous suspensions of unmodified granules typically ranges from 4.5 to 5.5, reflecting the amphoteric nature of surface hydroxyl groups 20.
Impurity levels are rigorously controlled to meet application-specific requirements. High-purity pyrogenic alumina granules contain >99.6 wt% Al₂O₃, with SiO₂ <0.1 wt%, Fe₂O₃ <0.2 wt%, and TiO₂ <0.1 wt% 20. Residual chloride content, a byproduct of AlCl₃ hydrolysis, is maintained below 0.5 wt% through post-synthesis washing 20.
Spray-drying represents the most widely adopted method for producing aluminium oxides granules with controlled size distribution and morphology. The process begins with dispersion of pyrogenic aluminium oxide powder (BET surface area 50–150 m²/g) in water at concentrations of 3–25 wt%, often supplemented with organic auxiliaries such as polyalcohols, polyethers, or fluorocarbon-based surfactants to enhance dispersion stability and modify particle morphology 36. The dispersion is atomized using disk or nozzle atomizers (single-fluid or two-fluid nozzles) at inlet temperatures of 170–300°C and outlet temperatures of 90–130°C 1619. The rapid evaporation of water results in spherical granules with average diameters of 5–150 μm and tamped densities of 300–1200 g/l 367.
Critical process parameters include:
Post-spray-drying treatments include heat treatment at 150–1000°C for 1–8 hours to adjust phase composition and mechanical strength 36, and silanization using halosilanes, alkoxysilanes, silazanes, or siloxanes to impart hydrophobicity 367. Silanization is typically performed by spraying the silanizing agent (optionally dissolved in ethanol) onto granules at room temperature, followed by heat treatment at 105–400°C for 1–6 hours 36.
For applications requiring larger granules (200–1500 μm), a dry compaction-crushing process is employed. Pyrogenic metal oxide powder with tamped density of 10–1200 g/l is compacted into slugs, which are subsequently crushed and classified 48. The slug fragments exhibit tamped densities of 210–2000 g/l, significantly higher than spray-dried granules 48. This method avoids wet processing, reducing contamination risk and simplifying production for high-purity applications. The process is applicable to oxides of Al, B, Ce, Cs, Er, Fe, In, Ga, Ge, Ni, Pb, Sn, Ta, Zr, and Zn 48.
Wet granulation involves mixing aluminium oxide suspension or sol with water-repellent agents (cationic or amphoteric type) and organic solvents poorly miscible with water, followed by phase separation, washing, drying, and calcination 1. This method produces granules with tailored surface chemistry but requires careful control of pH and ionic strength to prevent premature gelation. Sol-gel routes, though not detailed in the provided sources, offer precise control over phase purity and porosity but are more costly and time-consuming than pyrogenic methods.
A specialized process for active aluminium oxide involves decomposing aluminium oxide trihydrate in a steam-gas environment containing 13–15 wt% hydrogen at 350–500°C and 4–16 kPa, yielding amorphous aluminium oxide 2. The product is ground, sodium compounds are removed, and the material is plasticized at 125–132°C and pH 4 before granulation, drying, and baking 2. This method produces granules with high catalytic activity due to the amorphous structure and elevated surface area.
Granule quality is assessed through:
Aluminium oxides granules exhibit multimodal size distributions depending on production method. Spray-dried granules have average diameters of 5–150 μm 367, while compacted-crushed granules range from 200 to 1500 μm 48. The primary particles within granules measure 5–50 nm for pyrogenic alumina 36 and 10–600 nm for polishing-grade alumina 1112. Hexahedral primary particle morphology with aspect ratios of 1–5 is preferred for polishing applications to minimize scratching 1112. The mean aggregate diameter in aqueous dispersions is maintained below 100 nm through surface modification with organophosphonic acids and hydroxycarboxylic acids 13.
Tamped density, a measure of granule packing efficiency, varies from 50 g/l for highly porous granules 20 to 2000 g/l for densely compacted variants 48. Spray-dried granules typically exhibit tamped densities of 300–1200 g/l 367, while wet-granulated products range from 250 to 800 g/l 110. The relative density of the aluminium oxide phase is approximately 3.2 g/ml 20, with porosity inversely related to tamped density. High tamped density correlates with improved flowability and reduced dusting, critical for automated handling in industrial settings.
BET-specific surface area ranges from 20 m²/g for α-alumina-rich granules 10 to 200 m²/g for transition alumina granules 13. The surface area decreases with increasing calcination temperature due to sintering and phase transformation. Granules with BET surface areas of 50–150 m²/g are optimal for catalyst supports, balancing active site density with mechanical stability 3617. The absence of internal porosity in pyrogenic alumina granules distinguishes them from sol-gel or precipitated variants, which exhibit mesoporous or macroporous structures 36.
Transition aluminas (γ, δ, θ) transform to α-alumina at temperatures above 1000°C, with transformation kinetics influenced by particle size, impurities, and atmosphere 10. Treatment in hydrogen chloride or chlorine atmospheres at 800–1200°C for 0.5–5 hours accelerates α-alumina formation, yielding granules with ≥98 wt% α-phase and isolated particles of 1–50 μm diameter 10. The ignition loss (2 hours at 1000°C) is typically <3 wt%, reflecting low organic content and high thermal stability 20. Drying loss (2 hours at 105°C) is maintained below 5 wt% to ensure consistent performance in moisture-sensitive applications 20.
Aluminium oxides granules exhibit amphoteric behavior, with isoelectric points (IEP) around pH 8–9 for unmodified surfaces. The pH of aqueous suspensions ranges from 4.5 to 5.5 for pyrogenic alumina 20, reflecting surface hydroxyl group dissociation. Surface modification with organophosphonic acids shifts the IEP to lower pH values, enhancing dispersion stability in acidic media 13. Silanization with alkylsilanes or aminosilanes imparts hydrophobicity, with water contact angles exceeding 90° for octyl- or hexadecyl-modified granules 36.
The hardness of α-alumina granules approaches 9 on the Mohs scale, making them suitable for abrasive applications. Transition alumina granules exhibit lower hardness (6–7 Mohs) but higher friability, advantageous for polishing applications requiring controlled material removal rates 1112. The compressive strength of granules increases with tamped density and α-alumina content, with values exceeding 50 MPa for densely compacted granules 48.
Aluminium oxides granules serve as high-performance supports for heterogeneous catalysts in petrochemical refining, emissions control, and fine chemical synthesis. The high surface area (50–150 m²/g) and thermal stability of transition alumina granules provide abundant active sites and resistance to sintering at reaction temperatures up to 800°C 3617. Spray-dried granules with average diameters of 50–150 μm offer optimal balance between pressure drop and mass transfer in fixed-bed reactors 36. Surface modification with organophosphonic acids enhances metal precursor dispersion during catalyst preparation, improving activity and selectivity 13.
Case Study: Automotive Exhaust Catalysts — Automotive
Aluminium oxide granules modified with ceria and zirconia serve as supports for platinum-group metals in three-way catalytic converters. The granules' thermal stability at exhaust temperatures (400–900°C) and resistance to sulfur poisoning ensure long-term performance. Tamped densities of 600–900 g/l provide mechanical strength to withstand vibration and thermal cycling 36.
R&D Recommendations: Investigate hierarchical porosity through dual-templating to enhance diffusion of bulky reactants. Evaluate lanthanide doping to improve oxygen storage capacity and redox cycling stability.
Hexahedral aluminium oxide particles with aspect ratios of 1–5 and average primary particle sizes of 0.01–0.6 μm are employed in chemical-mechanical planarization (CMP) of silicon wafers, hard disk substrates, and display glass 1112. The α-conversion rate of 5–70% balances removal rate (higher for transition alumina) and surface finish (better for α-alumina) 1112. Polishing compositions containing 1–10 wt% aluminium oxide granules achieve removal rates of 100–500 nm/min with surface roughness (Ra) below 0.3 nm 1112.
Performance Metrics:
R&D Recommendations: Develop core-shell granules with soft transition alumina cores and hard α-alumina shells to optimize removal rate and minimize scratching. Explore pH-responsive surface coatings to enable selective polishing of multi-material stacks.
Silanized aluminium oxide granules with carbon contents of 0.3–12.0 wt% function as matting agents, oil absorbers, and texture modifiers in cosmetics 367. The hydrophobic surface reduces sebum shine in foundations and powders, while the spherical morphology imparts smooth application feel. Granules with average diameters of 5–20 μm are preferred for facial products to avoid visible particles 367.
Formulation Guidelines:
**Regulatory
| Org | Application Scenarios | Product/Project | Technical Outcomes |
|---|---|---|---|
| DEGUSSA AG (Evonik Degussa GmbH) | Catalyst supports for petrochemical refining and emissions control, cosmetic formulations as matting agents and oil absorbers, polishing abrasives for semiconductor and display substrates, and ceramic precursor materials. | AEROPERL® Alu Granules | Spray-dried pyrogenic aluminium oxide granules with controlled particle size (5-150 μm), tamped density (300-1200 g/l), and BET surface area (50-150 m²/g), enabling optimized dispersion stability and mechanical strength through surface modification. |
| FUJIMI INC. | Chemical-mechanical planarization (CMP) of silicon wafers, hard disk substrates, and display glass in semiconductor manufacturing, providing high selectivity (SiO₂/Si₃N₄ ratio 20:1-50:1) and minimal scratching. | Hexahedral Alumina Polishing Abrasives | Hexahedral primary particles with aspect ratio 1-5, average size 0.01-0.6 μm, and α-conversion rate 5-70%, achieving removal rates of 200-400 nm/min with surface roughness below 0.3 nm and defect density less than 0.1 defects/cm². |
| Evonik Degussa GmbH | High-purity applications requiring large granules with minimal contamination, including advanced ceramic manufacturing, high-performance catalyst supports, and specialty abrasive materials for industrial processing. | Coarse Metal Oxide Granules (Compaction-Crushing Process) | Dry compaction-crushing method producing granules with particle diameter 200-1500 μm and tamped density 210-2000 g/l, eliminating wet processing contamination while achieving superior packing efficiency and mechanical strength exceeding 50 MPa. |
| Evonik Degussa GmbH | Ink-absorbing coatings for inkjet media, high-performance catalyst preparation with improved metal precursor dispersion, and specialty coating compositions requiring stable nanoscale alumina dispersions. | Surface-Modified Alumina Dispersions | Pyrogenic aluminium oxide with BET surface area 50-150 m²/g, modified with organophosphonic acids and hydroxycarboxylic acids, achieving mean aggregate diameter below 100 nm and Sears/BET ratio 0.150-0.160 for enhanced dispersion stability. |
| Evonik Degussa GmbH | Plasma-sprayed protective coatings, thermal barrier systems, high-temperature insulation materials, and advanced ceramic components requiring exceptional purity and thermal stability up to 1000°C. | AEROPERL® Alu 100/30 | High-purity pyrogenic alumina granules (>99.6 wt% Al₂O₃) with BET surface area 100±15 m²/g, primary particle size 13 nm, and controlled impurities (SiO₂<0.1%, Fe₂O₃<0.2%), suitable for thermal spray applications and plasma coating processes. |