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Alumina & Aluminium Hydroxide Articles.

Calcined alumina and ATH grades for ceramics, refractories, flame retardants and polishing.

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Pseudo-Boehmite Gel Aging Failure: Why 72h Aging Produces Un-Peptizable Product and How to Recover the Batch | AluminaWorld
Alumina & ATH

Pseudo-Boehmite Gel Aging Failure: Why 72h Aging Produces Un-Peptizable Product and How to Recover the Batch | AluminaWorld

Engineering guide to pseudo-boehmite gel aging failure at 72 hours: surface dehydroxylation mechanism, four failure modes (over-temperature, mother-liquor…

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REACH SVHC Candidate List 2026 Update: Pseudo-Boehmite, ATH and ZSM-5 Status Check
Alumina & ATH

REACH SVHC Candidate List 2026 Update: Pseudo-Boehmite, ATH and ZSM-5 Status Check

Practical buyer-engineer guide to the REACH SVHC Candidate List 2026 update for pseudo-boehmite, aluminum hydroxide (ATH), and ZSM-5 zeolite. Includes…

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ATH for Polyurethane (PU) Foam: 30% vs 50% Loading — Cone Calorimeter HRR Data
Alumina & ATH

ATH for Polyurethane (PU) Foam: 30% vs 50% Loading — Cone Calorimeter HRR Data

Engineering guide to aluminium hydroxide (ATH) loading in flexible and rigid polyurethane foam. Cone calorimeter (ISO 5660-1) peak HRR and THR data at 30%…

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Calcined Alumina for Sapphire Crystal Growth (LED / Watch Industry): Na Impurity Limit <10 ppm Requirements
Alumina & ATH

Calcined Alumina for Sapphire Crystal Growth (LED / Watch Industry): Na Impurity Limit <10 ppm Requirements

Engineering guide to calcined alumina for sapphire crystal growth in LED and watch-industry applications: Na, K, Fe, Si, Ca impurity limits, alpha-Al2O3…

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Why Your Regeneration Cycle Keeps Getting Longer: 7 Root Causes Ranked by Frequency - AluminaWorld
Alumina & ATH

Why Your Regeneration Cycle Keeps Getting Longer: 7 Root Causes Ranked by Frequency - AluminaWorld

Regeneration cycle creep almost always has one of seven causes. The seven are listed below in descending order of field frequency. Two of them

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UN Packaging, IMDG and Dangerous Goods Classification for Adsorbents and Alumina Powders: What Exporters Get Wrong on the First Container | AluminaWorld
Alumina & ATH

UN Packaging, IMDG and Dangerous Goods Classification for Adsorbents and Alumina Powders: What Exporters Get Wrong on the First Container | AluminaWorld

Practical engineering guide to UN GHS, IMDG Code 41-22 and IATA DGR 65th classification for activated alumina, molecular sieve, ATH and pseudo-boehmite…

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Tabular Alumina T-60 vs T-64 vs White Fused Alumina for Ladle Lining Castables: Particle Packing, Water Demand, and 1450°C Bulk Density — Procurement Guide
Alumina & ATH

Tabular Alumina T-60 vs T-64 vs White Fused Alumina for Ladle Lining Castables: Particle Packing, Water Demand, and 1450°C Bulk Density — Procurement Guide

Procurement-grade comparison of tabular alumina T-60, T-64, and WFA grain for low-cement and ultra-low-cement castable ladle linings in iron and steel…

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Sole-Source vs Dual-Source Adsorbent Supply: Qualification Cost, Stock-Out Risk and Hidden Switching Cost Modelling | AluminaWorld
Alumina & ATH

Sole-Source vs Dual-Source Adsorbent Supply: Qualification Cost, Stock-Out Risk and Hidden Switching Cost Modelling | AluminaWorld

Procurement-engineer guide to choosing between sole-source and dual-source adsorbent supply. How to model qualification cost per kg, stock-out risk in…

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Sizing a Heatless (PSA) vs Heated Purge Air Dryer: Purge Loss Percentage and Energy Trade-Off | AluminaWorld
Alumina & ATH

Sizing a Heatless (PSA) vs Heated Purge Air Dryer: Purge Loss Percentage and Energy Trade-Off | AluminaWorld

Why adsorber vessels are designed with a bed length-to-diameter ratio between 3:1 and 5:1, what breaks outside that window — channelling, high pressure…

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Sizing a Heatless (PSA) vs Heated Purge Air Dryer: Purge Loss Percentage and Energy Trade-Off | AluminaWorld
Alumina & ATH

Sizing a Heatless (PSA) vs Heated Purge Air Dryer: Purge Loss Percentage and Energy Trade-Off | AluminaWorld

Engineering guide to heatless (PSA) vs heated-purge blower-purge air dryer sizing. ISO 7183 + ISO 8573-1 purge-loss formulas, desiccant volume sizing for…

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Reading a Failed Crush-Strength Report: ASTM D4179 Outliers vs Genuine Batch Rejection - AluminaWorld
Alumina & ATH

Reading a Failed Crush-Strength Report: ASTM D4179 Outliers vs Genuine Batch Rejection - AluminaWorld

Diagnostic framework for a failed ASTM D4179 single-bead crush-strength report on molecular sieve, activated alumina, and catalyst carrier CoAs: the 5…

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Reactive Alumina in Low-Soda Refractory Castables: Sintering Activity, Sodium-Defect Control, and Burned-Magnesia Bonding Chemistry
Alumina & ATH

Reactive Alumina in Low-Soda Refractory Castables: Sintering Activity, Sodium-Defect Control, and Burned-Magnesia Bonding Chemistry

Reactive alumina in low-soda refractory castables — sintering activity, sodium-defect control, MgO spinel bonding, dosing, and procurement specs.…

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Reactive Alumina for Epoxy Potting: 5N vs 3N Thermal Conductivity (W/mK) and CTE Data
Alumina & ATH

Reactive Alumina for Epoxy Potting: 5N vs 3N Thermal Conductivity (W/mK) and CTE Data

8500-word engineering guide: 5N vs 3N vs 4N reactive alumina in epoxy potting, k-model equations, viscosity, CTE, dielectric, 5 case studies (IGBT, EV…

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Pseudo Boehmite for Toothpaste Abrasive — RDA Value and Formulation | AluminaWorld
Alumina & ATH

Pseudo Boehmite for Toothpaste Abrasive — RDA Value and Formulation | AluminaWorld

Pseudo boehmite (AlOOH) is used as a low-abrasion polishing agent in premium toothpaste, replacing hydrated silica with controlled RDA (Relative Dentin…

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Post-Shutdown Bed Rewetting: Liquid Carryover Damage and the 48-Hour Recovery Procedure - AluminaWorld
Alumina & ATH

Post-Shutdown Bed Rewetting: Liquid Carryover Damage and the 48-Hour Recovery Procedure - AluminaWorld

Engineering protocol for restarting a water-flooded desiccant or molecular sieve bed after unplanned shutdown: distinguishing free water from chemisorbed…

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Loss on Ignition (LOI) vs Loss on Drying (LOD): The Spec Ambiguity That Causes Most Claims | AluminaWorld
Alumina & ATH

Loss on Ignition (LOI) vs Loss on Drying (LOD): The Spec Ambiguity That Causes Most Claims | AluminaWorld

Procurement-engineer guide to LOI and LOD on industrial adsorbents and alumina powders: why the two numbers cannot be substituted, the 4 reasons the spec…

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ISO 9277 BET Surface Area vs single-Point Method: Why Two Labs Report Different m²/g | AluminaWorld
Alumina & ATH

ISO 9277 BET Surface Area vs single-Point Method: Why Two Labs Report Different m²/g | AluminaWorld

Procurement-engineer guide to ISO 9277 BET multi-point vs single-point surface area measurement on activated alumina, molecular sieves and…

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Hydrogen Refuelling Station Adsorbent Selection: SAE J2719 Grade D Compliance at 700 bar - AluminaWorld
Alumina & ATH

Hydrogen Refuelling Station Adsorbent Selection: SAE J2719 Grade D Compliance at 700 bar - AluminaWorld

How to specify molecular sieve and activated alumina beds for hydrogen refuelling stations to meet SAE J2719 / ISO 14687 Grade D purity, including 700 bar…

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How to Audit an Adsorbent Supplier Remotely: 12 Documents to Request Before the First PO | AluminaWorld
Alumina & ATH

How to Audit an Adsorbent Supplier Remotely: 12 Documents to Request Before the First PO | AluminaWorld

Procurement-engineer guide to running a remote supplier audit on a Chinese or Asian adsorbent manufacturer. The 12 documents that close 80 percent of…

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Freight vs Density: Why Bulk Density Decides Your Landed Cost per Kg of Adsorption Capacity - AluminaWorld
Alumina & ATH

Freight vs Density: Why Bulk Density Decides Your Landed Cost per Kg of Adsorption Capacity - AluminaWorld

Two adsorbent drums with the same nominal capacity can carry very different freight cost per kg of working capacity. This procurement-engineering guide…

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Calcined Alumina in LTCC / HTCC Ceramic Substrates: Sintering Shrinkage Control Within +/-0.2% - AluminaWorld
Alumina & ATH

Calcined Alumina in LTCC / HTCC Ceramic Substrates: Sintering Shrinkage Control Within +/-0.2% - AluminaWorld

How calcined alumina (Al2O3) is formulated into low-temperature co-fired ceramic (LTCC) and high-temperature co-fired ceramic (HTCC) substrates, covering…

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Calcined Alumina for Sapphire Substrate Lapping and Polishing — Particle Size Selection | AluminaWorld
Alumina & ATH

Calcined Alumina for Sapphire Substrate Lapping and Polishing — Particle Size Selection | AluminaWorld

Calcined alumina (alpha-Al2O3) is the standard polishing abrasive for sapphire substrate (LED, watch face, semiconductor wafer) lapping and polishing.…

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CMP Slurry Settling: Pseudo-Boehmite vs Fumed Alumina for Sub-0.5 µm Polishing
Alumina & ATH

CMP Slurry Settling: Pseudo-Boehmite vs Fumed Alumina for Sub-0.5 µm Polishing

Engineering deep dive into pseudo-boehmite vs fumed alumina for CMP slurry at sub-0.5 micron nodes. Covers gel morphology, zeta potential envelope, LPC at…

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Alumina Powder for Thermal Interface Materials (TIM): Bimodal Packing to Reach 6 W/mK - AluminaWorld
Alumina & ATH

Alumina Powder for Thermal Interface Materials (TIM): Bimodal Packing to Reach 6 W/mK - AluminaWorld

How 3A and 5A molecular sieve beds are sized, regenerated, and qualified for removing moisture, CO2, and oxygenates from electronic-grade specialty gases…

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