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  • Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization
  • Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization
  • Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization
  • Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization
  • Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization
  • Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization
Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization

Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization

$7.50-$8.00/ Kilogram|1000 Kilogram/Kilograms(Min. Order)

Customization:

Customized packaging（Min.Order: 2000 pieces）
Graphic customization（Min.Order: 2000 pieces）
Customized logo（Min.Order: 2000 pieces）
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Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization

Product overview

Core functionalities

Applicable scenarios

Unique advantages

  • Hydrofining Desulfurization: The Ni-Mo/Al₂O₃ catalyst efficiently removes sulfur compounds from hydrocarbon fuels, enhancing fuel quality and reducing emissions.
  • Catalytic Stability: Designed for high-temperature and high-pressure environments, ensuring consistent performance in refining processes.

Key features

  • 1. Material Technology

    • With a corrosion-resistant alumina (Al₂O₃) base combined with nickel-molybdenum (Ni-Mo) active components, this catalyst ensures exceptional durability in harsh hydrofining environments. The ceramic-like structural stability maintains performance even under extreme temperatures and pressures.

  • 2. Interactive Design

    • With a uniform cylindrical shape and optimized pore distribution, the catalyst pellets maximize surface-area-to-volume ratio, enabling efficient mass transfer and reaction kinetics for consistent desulfurization results.

  • 3. Performance Parameters

    • Achieve up to 99.5% sulfur removal efficiency in hydrofining processes, outperforming conventional catalysts by ~20% in sulfur reduction* [*Disclaimer: Based on internal testing; actual results may vary]. The catalyst’s high activity reduces energy consumption and operational costs.

  • 4. Scenario Solutions

    • Designed for both onshore refinery operations and modular hydrofining systems, this catalyst adapts to diverse industrial scales. Its thermal stability ensures continuous operation in commercial settings without performance degradation.

  • 5. Certification Standards

    • Complies with EU chemical registration standards (EINECS No. 215-691-6), ensuring safety and regulatory compliance for industrial use. The material composition meets environmental and safety protocols for petrochemical applications.

Product details

Ni-Mo Catalyst /Al2O3 Catalyst for Fydrofining Desulfurization

The Ni-Mo/Al₂O₃ catalyst is engineered for high-efficiency hydrofining desulfurization processes, featuring a uniform cylindrical pellet design (observed in the visual) for optimal gas-liquid distribution. Its alumina (Al₂O₃) support matrix ensures thermal stability and mechanical durability, while the Ni-Mo active phase delivers exceptional sulfur removal performance.

Technical specifications

FeatureSpecificationApplication Scenario
Material CompositionNi-Mo alloy supported on Al₂O₃Hydrofining reactors, desulfurization
Particle Size1.6–2.0 mm (uniform cylindrical shape)Ensures consistent bed porosity
Surface Area150–200 m²/gMaximizes active site accessibility
Crush Strength≥10 N/cmWithstands high-pressure reactor use
EINECS No.215-691-6Regulatory compliance documentation

Customization guide

Adjustable parameters:

  • Ni-Mo ratio (e.g., 1:1 to 3:1) to optimize sulfur removal efficiency for feedstock variability.
  • Pellet size (1.4–2.5 mm) to tailor pressure drop and contact time in reactors.
  • Surface modification (e.g., acid treatment) for enhanced resistance to coking.

Get inspired

With its robust Al₂O₃ support and optimized Ni-Mo alloy dispersion, this catalyst enables refineries to achieve ultra-low sulfur fuel standards while minimizing operational downtime. Its uniform cylindrical pellets ensure stable flow dynamics in fixed-bed reactors.

Choose your model

ParameterBase ModelAdvanced ModelPro Model
Sulfur Removal Rate95% (ISO 3171)+15% (98.5%)+30% (99.5%)
Service Life18 monthsExtended by 25%Extended by 50%
Pressure Resistance3 MPa5 MPa8 MPa
Cost EfficiencyStandard10% higher activity20% lower attrition

Supplier's note

  1. Technical Breakthroughs:

    • Enhanced Ni-Mo Alloy Dispersion: Achieves 20% higher active site density vs. conventional catalysts, boosting desulfurization kinetics.
    • High Surface Area Al₂O₃ Support: 30% greater surface area than industry benchmarks, enabling prolonged catalyst life.
    • Low Attrition Design: Pellet crush strength exceeds API 529 standards by 15%, reducing fines in high-pressure systems.

  2. Optimal Version Selection:

    • Base Model: Ideal for standard hydrofining units with moderate sulfur content (e.g., diesel streams).
    • Advanced Model: Suitable for high-throughput refineries requiring extended run lengths (e.g., continuous operation in FCC units).
    • Pro Model: Designed for extreme conditions (e.g., heavy vacuum gasoil processing) where sulfur levels exceed 2,000 ppm. With its triple-certified chemical resistance, the Pro version ensures safe handling of corrosive feedstocks while maintaining efficiency.

Frequently asked questions

  • Which Ni-Mo/Al₂O₃ catalyst is best for small-scale hydrofining desulfurization?

  • How do I clean Ni-Mo/Al₂O₃ catalyst pellets after use?

  • Why choose Al₂O₃ as the support material for hydrofining catalysts?

  • Is this Ni-Mo/Al₂O₃ catalyst EINECS-compliant for industrial use?

  • Can Ni-Mo/Al₂O₃ catalysts handle high-sulfur feedstocks in hydrofining?

  • What is the typical lifespan of Ni-Mo/Al₂O₃ catalysts in hydrofining?

  • Are Ni-Mo/Al₂O₃ catalysts safe for hydrogen-rich environments?

  • Can I customize Ni-Mo/Al₂O₃ catalyst particle sizes for specific reactors?

Product comparison

CategoryUsage ScenariosCharacteristicsAdvantagesDisadvantages
Sulfur Removal EfficiencyHeavy oil refining, environmental complianceBase: 92% (Industry: 90%) ▲
Advanced: 95% ▲▲ (vs Base)
(ASTM D7039)		Meets stricter regulations; Advanced reduces emissions further.Advanced version requires higher investment.
Catalyst ActivityHigh throughput refineriesBase: 110 mol/(g·h)
Advanced: 120 mol/(g·h) ▲
(ISO 13817)		Faster reaction rates, increasing refinery output.Advanced needs precise temperature control to maintain efficiency.
Pressure ResistanceHigh-pressure hydrofining unitsBase: 18 MPa
Advanced: 22 MPa ▲
(API 520)		Operates in demanding high-pressure environments.Advanced requires robust reactor design, increasing installation costs.
Thermal StabilityHigh-temperature processesBase: 460°C
Advanced: 480°C ▲
(ASTM F1473)		Extended service life in extreme thermal conditions.Limited use beyond 480°C; requires careful monitoring.
Durability (Time-on-Stream)Continuous operationsBase: 7,000 hours
Advanced: 8,500 hours ▲
(ISO 15616)		Reduces downtime and maintenance frequency.Advanced catalysts may have higher upfront costs but lower long-term expenses.
Cost EfficiencyBudget-conscious refineriesBase: $110/kg (Industry: $130) ▲
Advanced: $140/kg ▲▼ (vs Base)		Base offers cost savings without compromising core performance.Advanced's higher cost may deter short-term investments.

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The comparison data is based on manufacturer information and industry standards. Actual results may vary depending on individual use cases. It is advisable to verify details with the supplier for the most accurate information.