
Technical Indicators | Detailed Specifications | Remarks |
Active Components | Pt, Pd, Rh, Ce, La, Pr | Rh-Pt-Pd ternary system with rare earth modifiers |
Noble Metal Loading | 0.3-1.2g/L | Higher Rh ratio (15-20% of total noble metals) for sulfur tolerance |
Support Material | TiO₂-Al₂O₃ Composite (La-Pr modified) | High sulfur adsorption capacity, 200-300cpi |
Appearance Dimensions | Standard 10010050mm/15015050mm, customizable | Compatible with RCO/RTO systems for sulfur-containing gas |
Bulk Density | 580±50g/L | Ensures stable bed operation in corrosive environments |
Operating Temperature Range | 280~500℃ | Optimal reaction interval: 320-400℃ |
Maximum Short-term Temperature Resistance | 850℃ | Resists thermal shock from sulfur oxidation exotherm |
Gas Hourly Space Velocity (GHSV) | 8000~18000h⁻¹ | Adaptable to sulfur-containing gas with variable concentrations |
Purification Conversion Rate | >95% (in 100ppm H₂S environment) | Benzene series treatment efficiency: 97%+ |
Sulfur Tolerance Capacity | ≤300ppm (H₂S equivalent) | Maintains activity for 6+ months in 50ppm H₂S |
Compressive Strength | ≥12MPa | Corrosion-resistant, non-friable |
Specific Surface Area | ≥250m²/g | Enhances sulfur adsorption and active site exposure |
Sulfur Adsorption Capacity | ≥5mg/g | Captures sulfur species to protect active sites |
Storage Conditions | Sealed, dry environment; avoid sulfur-containing gases | Shelf life: 12 months (unopened) |
Superior Sulfur Tolerance: The La-Pr modified TiO₂-Al₂O₃ support forms Lewis acid sites that selectively adsorb sulfur compounds (H₂S, thiophene) through chemical bonding, preventing them from diffusing to noble metal active sites. Rhodium (Rh) forms Rh-S bonds with low stability, which can be oxidized and desorbed during catalyst regeneration, avoiding permanent poisoning. Even in gas streams with 100ppm H₂S, the catalyst maintains ≥95% VOC conversion efficiency for over 6 months, far exceeding the 3-6 month service life of traditional catalysts.
Dual-Function Purification: It achieves simultaneous removal of VOCs and sulfur-containing impurities without additional desulfurization equipment. Sulfur compounds are adsorbed and oxidized to harmless SO₂ (which can be further treated by downstream desulfurization units), while VOCs are converted to CO₂ and H₂O. This dual-function design simplifies the waste gas treatment process, reduces system footprint, and cuts initial investment by 30% compared to "desulfurization + catalytic oxidation" combined systems.
High Catalytic Activity & Stability: The Rh-Pt-Pd ternary active system synergistically enhances catalytic performance—Pt optimizes oxidation of oxygen-containing VOCs, Pd improves activity for aromatics and alkanes, and Rh boosts sulfur tolerance and thermal stability. The La-Pr modified support inhibits sintering of noble metal particles (maintaining particle size at 2-5nm even after 1000 hours of operation) and enhances coating adhesion, ensuring long-term structural stability with compressive strength ≥12MPa.
Wide Adaptability to Working Conditions: It tolerates sulfur concentration fluctuations (10-300ppm H₂S equivalent) and adapts to VOC concentrations ranging from 500 to 10,000mg/m³. The operating temperature range of 280-500℃ accommodates thermal fluctuations in industrial processes, while the GHSV range of 8000-18000h⁻¹ allows flexible adjustment based on gas flow and composition. It also resists poisoning from chlorine-containing impurities (≤50ppm) and high humidity (relative humidity ≤90%), making it suitable for complex industrial environments.
Easy Regeneration & Low Maintenance: When sulfur adsorption reaches saturation (indicated by a 10% drop in purification efficiency or 50℃ rise in light-off temperature), the catalyst can be regenerated by heating to 450-500℃ and purging with air containing 5-10% oxygen for 2-4 hours. This regenerative process can be repeated 3-5 times, extending the overall service life to 2-3 years. Daily maintenance only requires regular inspection of bed pressure drop and purification efficiency, with no need for water washing or chemical treatment.
Technological Innovation in Anti-Sulfur Design: The unique "three-layer structure" (sulfur barrier layer, active component layer, sulfur adsorption layer) and Rh-Pt-Pd ternary system address the root cause of sulfur poisoning. Compared to traditional catalysts that simply increase noble metal loading, this design achieves a 5x improvement in sulfur tolerance while reducing noble metal usage by 10-15%, balancing performance and cost.
Total Cost of Ownership Advantage: By eliminating the need for pre-desulfurization equipment (e.g., activated carbon adsorption towers, chemical scrubbers), it reduces initial investment by 30%+. The 2-3 year service life (6x longer than traditional catalysts in sulfur-containing environments) and regenerable design lower replacement and maintenance costs by 40% annually. Low-temperature operation (280-400℃ optimal) further reduces energy consumption by 20% compared to high-temperature anti-sulfur catalysts.
Strong Compatibility with Existing Systems: The standard honeycomb dimensions (10010050mm/15015050mm) and customizable design allow direct replacement of traditional catalysts in existing RCO/RTO units without modifying equipment structure. This enables enterprises to upgrade their waste gas treatment systems with minimal downtime and investment.
Compliance with Strict Environmental Standards: It meets international emission standards (e.g., EU REACH, US EPA) and Chinese national standards (GB 31570-2015, GB 31571-2015), with VOC emission concentrations ≤30mg/m³ and sulfur dioxide emission ≤50mg/m³. It helps enterprises in petrochemical, coking, and other high-pollution industries achieve ultra-low emissions and avoid environmental fines.
Treatment of sulfur-containing VOCs from crude oil distillation, catalytic cracking, and alkylation processes (e.g., benzene, toluene, xylene, and mercaptans).
Application in RCO units for waste gas from storage tanks, loading/unloading operations, and chemical synthesis workshops.
Typical sulfur concentration: 50-200ppm H₂S equivalent; VOC concentration: 1000-5000mg/m³.
Abatement of VOCs and sulfur-containing compounds from coal gasification, coking, and coal tar processing (e.g., phenols, naphthalene, H₂S, thiophene).
Suitable for waste gas treatment in coke oven gas purification, methanol synthesis, and ammonia production processes.
Typical sulfur concentration: 100-300ppm H₂S equivalent; VOC concentration: 2000-8000mg/m³.
Treatment of sulfur-containing organic waste gas from pesticide, dye, and pharmaceutical synthesis (e.g., thiols, thioethers, and aromatic hydrocarbons).
Application in processes involving sulfur-containing raw materials or intermediates, such as mercaptan synthesis and sulfonation reactions.
Typical sulfur concentration: 10-100ppm H₂S equivalent; VOC concentration: 500-3000mg/m³.
Leather & Tanning Industry: Treatment of waste gas from leather tanning and finishing (e.g., aldehydes, ketones, and sulfur-containing odorants).
Food Processing Industry: Purification of sulfur-containing VOCs from food fermentation and flavoring processes (e.g., hydrogen sulfide from protein decomposition).
Waste Incineration Plants: Treatment of sulfur-containing VOCs and dioxins precursors in flue gas (after dust removal and denitrification).
Q: What is the maximum sulfur concentration the catalyst can tolerate?
Q: How often does the catalyst need regeneration, and what is the regeneration process?
Q: Can the catalyst be used in gas streams containing both sulfur and chlorine impurities?
Q: What is the difference between this catalyst and traditional anti-sulfur catalysts?
Q: How to determine if the catalyst needs replacement instead of regeneration?
Q: What are the key precautions for storage and transportation?
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