Catalytic Activity | High Selectivity And Conversion Rate |
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Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
Pore Volume | 0.8-1.2 Cm3/g |
Moisture Content | Less Than 1% |
Thermal Stability | Up To 1000°C |
Regenerability | Can Be Regenerated Multiple Times Without Significant Loss Of Activity |
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Stability | Excellent Stability Under Harsh Conditions |
Pore Size | Uniform Pore Size Distribution |
Operating Temperature | 30-35°C |
Application | Selective Hydrogenation Of C3 Hydrocarbons |
Catalyst Type | Supported Metal Catalyst |
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Shape | Spherical |
Activity | High Activity For C3 Hydrogenation |
Stability | Excellent Stability Under Harsh Conditions |
Pore Size | Uniform Pore Size Distribution |
Bulk Density | 0.65-0.75 G/cm3 |
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Hydrogenation Selectivity | ≥ 95% |
Operating Temperature | 150-250°C |
Particle Size | 1.5-3.0 Mm |
Surface Area | ≥ 150 M2/g |
Surface Area | High Surface Area For Efficient Catalytic Activity |
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Pore Size | Uniform Pore Size Distribution |
Stability | Excellent Stability Under Harsh Conditions |
Particle Size | Narrow Particle Size Distribution |
Operating Temperature | 30-35°C |
Bulk Density | 0.65-0.75 G/cm3 |
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Catalyst Lifespan | ≥ 3 Years |
Surface Area | ≥ 150 M2/g |
Hydrogenation Selectivity | ≥ 95% |
Operating Pressure | 1-10 MPa |
Surface Hydroxyl Groups | High Concentration Of Surface Hydroxyl Groups |
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Application | Catalyst For Dehydrogenation Of Long Chain Alkanes |
Moisture Content | Less Than 1% |
Pore Volume | 0.8-1.2 Cm3/g |
Surface Area | 150-170 M2/g |
Active Metal | Palladium |
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Catalyst Type | Heterogeneous |
Thermal Stability | High |
Particle Size | 1-3 Mm |
Selectivity | >95% |
Catalyst Lifespan | ≥ 3 Years |
---|---|
Operating Temperature | 150-250°C |
Hydrogenation Selectivity | ≥ 95% |
Particle Size | 1.5-3.0 Mm |
Pore Volume | ≥ 0.35 ML/g |
Operating Pressure | 1-10 MPa |
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Surface Area | ≥ 150 M2/g |
Active Component Loading | ≥ 2 Wt% |
Pore Volume | ≥ 0.35 ML/g |
Support Material Content | ≥ 90 Wt% |