HT201 Type Organic Sulfur Hydrogenation Catalyst
HT201 type hydrogenation catalyst is prepared through total impregnation technique by using of high-quality carrier. It has features of even distribution of active ingredient, high strength, fine activity and long serve life. It is suitable for hydrogen manufacturing device and hydrodesulfurization device in smeltery, synthesis ammonia factory and organic synthesis plant.
Appearance | Straightness mm | Length mm | Bulk density kg/L | Active constituent% | Activity | Compression strength | End-use temperature ℃ |
dusty blue stripe or ball shape | Φ3~5 | 4-10 | 0.65-0.85 | Co-Mo | organic sulfur conversion rate ＞96% | stripe≥80N/cm | 230-400 |
Working pressure (Mpa) | gas space velocity (H-1) | liquid space velocity (H-1) | H2/ oil | arsenic in raw material gas (ppm) | organic suplhur in raw material gas or hydrocarbon (ppm) | S content in raw material(ppm) | Ci in raw material(ppm) |
1.0-4.0 | 1000-3000 | 1.0-6.0 | 80-100 | ＜100 | 100-200 |
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HT201-1 Type Organic Sulfur Hydrogenation Catalyst
HT 201-1 type hydrogenation catalyst is prepared through total impregnation technique by taking Co-Mo-Ni as active constituent and adding of special auxiliaries. It has features of high activity, fine strength, fine low-temperature property and high organic sulfur conversion capacity. It is suitable for hydro-conversion of organic sulfur in natural gas, oil field gas, coking dry gas and ligh toil in synthesis ammonia plant, methyl alcohol plant, carbon chemical plant and refining plant.
Appearance | Straightness mm | Length mm | Bulk density kg/L | Active constituent% | Activity | Compression strength | End-use temperature ℃ |
dusty blue stripe or ball shape | Φ3~5 | 4-10 | 0.65-0.85 | Co-Mo-Ni | organic sulfur conversion rate ＞96% | stripe≥80N/cm | 230-400 |
Working pressure (Mpa) | gas space velocity (H-1) | liquid space velocity (H-1) | H2/ oil | arsenic in raw material gas (ppm) | organic suplhur in raw material gas or hydrocarbon (ppm) | S content in raw material(ppm) | Ci in raw material(ppm) |
1.0-4.0 | 1000-3000 | 1.0-6.0 | 80-100 | ＜100 | 100-200 |
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HF101 Type Methanol Decomposition Hydrogen Production Catalyst
HF101 type methanol decomposition hydrogen production catalyst is used in reaction for preparation of H2+C02 from methyl alcohol water vapor method. It is copper-zinc series catalyst taking CuO as main part, ZnO, Al203 as internal part. It has features of large surface area of efficient copper, fine activity and stability, large pore volume and excellent pore size distribution. It is among leading level among both domestic and abroad like products.
Appearance | Specification mm | Bulk specific weight kg/L | CuO % content | ZnO % content | Al203 % content | Even crushing strength N/piece |
black cylinder with metallic lustre | 5±0.5 | 1.25-1.35 | ≥68 | ≥20 | ≥8 | ≥150 |
HT203 Type Hydrogenation Dearsenification Catalyst
HT 201-1 type hydrogenation catalyst is prepared through total impregnation technique by taking Co-Mo-Ni as active constituent and adding of special auxiliaries. It has features of high activity, fine strength, fine low-temperature property and high organic sulfur conversion capacity. It is suitable for hydro-conversion of organic sulfur in natural gas, oil field gas, coking dry gas and ligh toil in synthesis ammonia plant, methyl alcohol plant, carbon chemical plant and refining plant.
Appearance | Straightness mm | Length mm | Bulk density kg/L | Active constituent% | Activity | Compression strength | End-use temperature ℃ |
dusty blue stripe or ball shape | Φ3~5 | 4-10 | 0.65-0.85 | Co-Mo-Ni | organic sulfur conversion rate ＞96% | stripe≥80N/cm | 230-400 |
Working pressure (Mpa) | gas space velocity (H-1) | liquid space velocity (H-1) | H2/ oil | arsenic in raw material gas (ppm) | organic suplhur in raw material gas or hydrocarbon (ppm) | S content in raw material(ppm) | Ci in raw material(ppm) |
1.0-4.0 | 1000-3000 | 1.0-6.0 | 80-100 | ＜100 | 100-200 |
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HZ119 Type Ammonia Decomposition Dydrogen Manufacturing Catalyst
HZ119 type catalyst is sintering conversion catalyst taking nickel as active constituent, aluminium oxide and calcium aluminate as carrier. It is suitable for batch-type conversion of natural gas, partial partial oxidation of ammonia from light weight hydrocarbon or synthesis gas of methyl alcohol. It is also for preparation of reducing hydrogen gas and protective gas nitrogen gas.
Appearance | Straightness mm |
| Bulk density kg/L | Active constituentNiO% | Working pressure MPa | Compression strength | End-use temperature ℃ |
black and gray color cylinder or other special shape | Φ16x16x6 Φ19x19x9 |
| ~1.0 | ≥14 | normal pressure~5.0 | ≥350N/piece | 800~1000 |
Ni-Al Alloy Powder, Skeletal Ni Catalyst
Nickel aluminium catalyst is prepared through high-temperature fushing of electrolytic nickel and electrolytic aluminium. It has features of high activity, fine thermal conductivity, high mechanical strength and etc. It is for hydrogenation of unsaturated hydrocarbon, for dehydrogenation, desulfuration, dehalogenation.
Appearance | Diameter mm | Bulk specific weight kg/L | Active constituent% | Activity | Compression strength | End-use temperature ℃ |
black particle | 20-400 | 2.5-4.0 | nickel 30-50 | hydrogen absorption capacity＞500H2ml/g |
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HPA Type Efficient Pd-Al Catalyst
HPA type efficient Pd-Al catalyst is a kind of widely applied multi-functional catalyst. It is suitable for deep deoxygenization purification of various gases, such as, hydrogen, nitrogen and argon. Due to high catalytic activity, simple technique and high safety, it is widely applied in metallurgy, light industry, electronic and chemical department.
Appearance | Diameter mm | Pb content % | Bulk density g/ml | Anti-crush strength N/piece | Space velocity under room temperature | Nitrogen content |
ball shape | Φ3-5 | 0.1-1 | 0.6-0.8 | ≥120 | 5000-20000 | 1-2.5% to 1ppm or below |