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Catalyst

  • High quantity Methanol Cracking(Reforming) catalyst

    High quantity Methanol Cracking(Reforming) catalyst

    • Shape: Cylinder
    • Drying Method: Static Drying
    • Desiccant: Chemical Desiccant
    • Model NO: Steam Reformer Catalyst
    • Bulk Density: ≤1.3kg/cm3
    • Crushing strength: ≥80N/cm
    • CuO(Wt%): ≥65.0
    • ZnO(Wt%): ≥8.0
    • Al2O3(Wt%): ≥8.0
    • Other promoter(Wt%): ≥2.0
    • Loss on ignition (540℃/hr): ≤13.0
  • New Type of Decomposition Catalyst for Hydrogen Production

    New Type of Decomposition Catalyst for Hydrogen Production

    • Shape: Cylinder
    • Drying Method: Static Drying
    • Desiccant: Chemical Desiccant
    • Model NO: Steam Reformer Catalyst
    • Bulk Density: 0.9~1.0 Kg/L
    • NiO Content: ≥ 14.00 Wt%
    • Al2O3+Additives: The Balance Wt%
    • Loss on Ignition: ≤ 20 Wt%
    • Radial Crushing Strength of Particles: ≥ 300 N/ P
    • Pressure: 0.01MPa – 0.10MPa
    • Temperature: 750℃-850℃
    • Specification: 19 × 19 × 9 (mm)
    • HS Code: 3824999999
  • Steam Reformer Catalyst/Steam Reforming Catalyst Decomposition Catalyst for Hydrogen Production

    Steam Reformer Catalyst/Steam Reforming Catalyst Decomposition Catalyst for Hydrogen Production

    • Shape: Cylinder
    • Drying Method: Static Drying
    • Desiccant: Chemical Desiccant
    • Model NO: Steam Reformer Catalyst
    • Bulk Density: 0.9~1.0 Kg/L
    • NiO Content: ≥ 14.00 Wt%
    • Loss on Ignition: ≤ 20 Wt%
    • The Percentage of Low Strength Particles: ≤5.0%
    • Specification: 19 × 19 × 9 (mm)
    • HS Code: 3824999999
  • NaY Molecular Sieve High Silicon Aluminum Faujasite Cage Structure

    NaY Molecular Sieve High Silicon Aluminum Faujasite Cage Structure

    • Sorbent: Molecular Sieves
    • Shape: Balls
    • Drying Method:Static Drying
    • Desiccant: Chemical Desiccant
    • Relative Crystallinity: 92%
    • Lattice Constant(×10-10m): 24.65
    • Silica-Alumina Ratio(Molar Ratio): 5.2
    • Na2O Concent: 11.8%
    • BET Surface: 715 m2/g
    • Average Igloss: 22.48%
    • HS Code: 3824999999
  • 13X Molecular Sieve Used as Catalyze Carrier

    13X Molecular Sieve Used as Catalyze Carrier

    • Sorbent: Molecular Sieves
    • Shape: Balls
    • Drying Method:Static Drying
    • Desiccant: Chemical Desiccant
    • Particle Size: 1.5-1.7mm
    • Size Ratio to Grade: ≥98
    • Bulk Density: ≥0.64 g/ml
    • Wear Ratio: ≤0.20%
    • Crushing Strength: ≥30N/cm
    • H2O Adsorption: ≥25%
    • Static Co2adsorption: ≥17%
    • Packing Water: ≤1.5%
    • Transport Package: 1kg/Bag
    • HS Code: 3824999999
  • 5A Molecular Sieve Used for Desorption of Water, Carbon Dioxide in Psa Industry

    5A Molecular Sieve Used for Desorption of Water, Carbon Dioxide in Psa Industry

    • Sorbent: Molecular Sieves
    • Shape: Balls
    • Drying Method:Static Drying
    • Desiccant: Chemical Desiccant
    • Particle Size: 1.5-1.7mm
    • Size Ratio to Grade: ≥98
    • Bulk Density: ≥0.60 g/ml
    • Wear Ratio: ≤0.20%
    • Crushing Strength: ≥30N/cm
    • H2O Adsorption: ≥22%
    • Packing Water: ≤1.5%
    • Transport Package: 1kg/Bag
    • HS Code: 3824999999
  • 4A Molecular Sieve Used for Dryness of Impurity

    4A Molecular Sieve Used for Dryness of Impurity

    • Sorbent: Molecular Sieves
    • Shape: Balls
    • Drying Method:Static Drying
    • Desiccant: Chemical Desiccant
    • Particle Size: 1.5-1.7mm
    • Size Ratio to Grade: ≥98
    • Bulk Density: ≥0.60 g/ml
    • Wear Ratio: ≤0.20%
    • Crushing Strength: ≥30N/cm
    • H2O Adsorption: ≥20.5%
    • Packing Water: ≤1.5%
    • Transport Package: 1kg/Bag
    • HS Code: 3824999999
  • 3A Molecular Sieve Used for Dryness of Gas, Liquid

    3A Molecular Sieve Used for Dryness of Gas, Liquid

    • Sorbent: Molecular Sieves
    • Shape: Balls
    • Drying Method:Static Drying
    • Desiccant: Chemical Desiccant
    • Particle Size: 3-5mm
    • Silica-Alumina Ratio: 2
    • Compressive Strength: ≥90N
    • Static Water Adsorption: ≥20%
    • Bulk Density: ≥ 0.70g/Ml
    • Abrasion: ≤ 0.20%
    • Loss on Ignition: ≤1.50%
    • Transport Package: 1kg/Bag
    • HS Code: 3824999999
  • 5A Molecular sieve for hydrogen production Alkali metal silicaluminate

    5A Molecular sieve for hydrogen production Alkali metal silicaluminate

    • Particle size (mm): 2-3
    • Bulk density (g/ml): ≥ 0.75
    • Compressive strength (N): ≥40
    • Static water adsorption (%, wt): ≥21
    • Static nitrogen adsorption(%, wt): ≥11
    • Static carbon monoxide adsorption (%, wt): ≥27
    • Static n-hexane adsorption(%, wt): ≥14
    • Package water content(%):≤ 1.5
    • Particle conformance(%): ≥97
  • High Quantity Pre-Reformer Catalyst/Steam Reforming Catalyst For Production Of Synthesis Gas

    High Quantity Pre-Reformer Catalyst/Steam Reforming Catalyst For Production Of Synthesis Gas

    • Appearance: Granules
    • Particle size: ∮5×5mm
    • Purity: 42%/50%, Nickel Content(Ni) ≥50%
    • Minimum Order: Depends on your requirement
    • Model NO.: Pre-reformer catalyst
    • Carrier: Al2O3
    • Bulk density: 1.0-1.1kg/L
    • Chemical State: Reduced State and Stabilization
    • HS Code: 3815900000
    • Type: Steam Reforming Catalyst
  • Factory supply DME-1 Dimethyl ether catalyst for produce dimethyl ether

    Factory supply DME-1 Dimethyl ether catalyst for produce dimethyl ether

    • Appearance: White or light yellow extrudate
    • Chemical composition: Main components is Al203
    • Size: Diameteo3~4mm ,long:3~20mm
    • Bulk density: 0.45~0.50 kg/L
    • Specific surface area: ≥250m2/g
    • Average crushing strength: radial>80N/cm
    • Abrasion: ≤5%
  • 3A/4A/5A Molecular sieve used in Desiccant

    3A/4A/5A Molecular sieve used in Desiccant

    • Silica-Alumina ratio: 2
    • Diameter (mm): 3-5
    • Static water adsorption (%, wt): ≥20
    • Bulk density (g/ml): ≥ 0.70
    • Compressive strength (N): ≥90
    • Abrasion (%, wt): ≤ 0.20
    • Loss on ignition (%,wt): ≤1.50
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