
Technical Indicators | Detailed Specifications | Remarks |
Support Material | Alumina, silica, zeolite, activated carbon, TiO₂ | Application-dependent selection |
Active Components | Pt, Pd, Rh, Ni, Cu, Fe, V₂O₅, WO₃, etc. | Loading: 0.1-10wt% (customizable) |
Particle Shape | Spherical, cylindrical, irregular | Spherical preferred for fluidized beds |
Particle Size Range | 1-10mm (2-6mm most common) | Customizable for reactor type |
Specific Surface Area (BET) | 100-1500m²/g | 500-1200m²/g for adsorption-catalysis |
Total Pore Volume | 0.3-1.5cm³/g | Meso-pore dominated (2-50nm) for mass transfer |
Average Pore Diameter | 2-50nm | Optimized for reactant/product diffusion |
Bulk Density | 600-1200g/L | Dependent on support and porosity |
Crushing Strength | ≥50N/cm (cylindrical); ≥100N/particle (spherical) | Resists mechanical stress in reactors |
Operating Temperature Range | 150-800℃ | 150-400℃ (VOCs); 300-800℃ (reforming) |
Maximum Short-Term Tolerance | 900℃ | Withstands transient temperature spikes |
Gas Hourly Space Velocity (GHSV) | 500-20,000h⁻¹ | Fixed beds: 500-5,000; fluidized beds: 5,000-20,000 |
Catalytic Efficiency | ≥90% (VOCs); ≥95% (CO); ≥85% (NOx); ≥98% (synthesis) | Standard operating conditions |
Thermal Stability | ≤10% activity loss after 1000h at max temp | Resists sintering and phase change |
Poisoning Resistance | S/Cl/F tolerance (≤100ppm) | Enhanced by CeO₂/La₂O₃ dopants |
Service Life | 1-5 years (industrial conditions) | Dependent on reaction severity/impurities |
Storage Conditions | Sealed, dry (5-35℃); avoid moisture/corrosives | 12-month shelf life (unopened) |
Versatile Particle Design: Spherical/cylindrical/irregular shapes and 1-10mm size range adapt to fixed/fluidized/moving-bed reactors, enabling seamless process integration without custom equipment.
Optimized Pore Structure: 2-50nm average pore diameter and 0.3-1.5cm³/g pore volume balance active site exposure and mass transfer, critical for fast, efficient reactions.
Mechanical Robustness: Crushing strength ≥50N/cm (cylindrical) resists attrition, compression, and abrasion in industrial reactors, minimizing catalyst loss and maintenance downtime.
Broad Catalytic Compatibility: Supports diverse active components for VOCs oxidation, NOx reduction, hydrogenation, and chemical synthesis—adapting to varied industrial needs.
Scalable Performance: Consistent activity across particle sizes and batches enables scaling from pilot to industrial scale (10-100,000 Nm³/h gas flow) without performance degradation.
Cost-Effective Production: Mature manufacturing processes (extrusion, tableting) reduce costs by 30-50% vs. monolithic catalysts, ideal for high-volume applications.
Easy Replacement & Handling: Granular form allows gravity/pneumatic loading/unloading; spent catalyst is easily recovered for regeneration or disposal.
vs. Monolithic/Honeycomb Catalysts: 30-50% lower production cost, easier replacement (no reactor disassembly), and compatibility with existing granular reactor infrastructure—reducing retrofitting expenses.
vs. Powder Catalysts: Higher mechanical strength (no dust generation), lower pressure drop (avoids filter clogging), and simplified handling in industrial-scale operations.
Process Flexibility: Adapts to fixed-bed (high conversion), fluidized-bed (uniform temperature), and moving-bed (continuous regeneration) systems—covering diverse industrial requirements.
Customization Capability: Tailorable particle size, shape, active component loading, and pore structure for specific reactions (e.g., low-temperature VOCs oxidation, high-temperature reforming).
Cost-Efficient Lifecycle: 1-5 years service life and regenerability (thermal/chemical treatment) lower replacement frequency and total ownership cost vs. single-use catalysts.
VOCs Abatement: Pt/Pd-based spherical pellets (2-6mm) oxidize benzene, toluene, and solvents in petrochemical, coating, and printing industries (fixed-bed reactors, 200-400℃, ≥90% efficiency).
NOx Reduction: V₂O₅-WO₃/TiO₂ cylindrical pellets (3-5mm) for SCR systems in power plants, boilers, and diesel exhaust (300-400℃, ≥85% conversion).
CO Oxidation: Cu/Fe-based irregular pellets (1-3mm) in mining, metallurgy, and automotive auxiliary systems (150-300℃, ≥95% conversion).
Hydrogenation/Hydrogenolysis: Ni/Pt-based spherical pellets (4-8mm) for vegetable oil hydrogenation, aromatic hydrogenation, and ammonia synthesis (fixed-bed, 300-500℃).
Dehydrogenation/Reforming: Pt-Sn/Al₂O₃ pellets (2-4mm) for propane dehydrogenation (propylene production) and steam methane reforming (hydrogen production, 600-800℃).
Acid-Catalyzed Reactions: Zeolite pellets (3-6mm) for alkylation, isomerization, and catalytic cracking in oil refining (400-600℃).
Fuel Cell Catalysts: Pt/C pellet catalysts (1-2mm) for hydrogen purification and reformer gas treatment in fuel cell systems (200-300℃).
Biogas Upgrading: Ni-based pellets (4-6mm) remove CO₂ and H₂S from biogas, producing renewable natural gas (fixed-bed, 300-400℃).
Wastewater Treatment: TiO₂-based photocatalytic pellets (2-5mm) for organic pollutant degradation in advanced oxidation processes (ambient temperature).
Q: How to select particle size and shape for my reactor?
Q: What factors affect catalyst service life?
Q: Can pellet catalysts be regenerated?
Q: How does it compare to honeycomb catalysts in VOCs treatment?
Q: Storage and handling precautions?
Q: Are pellet catalysts suitable for high-pressure reactions?
Q: How to dispose of spent pellet catalysts?
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