Reforming Catalysts
Manufactured according to Specification TU 20.59.56-29-44912618-2018
Composition:
γ-alumina-supported platinum with special promoters
Catalysts AP-56, AP-64 are used in catalytic reforming process to produce high-octane gasoline components.
Specifications
Physical Properties | |
---|---|
Parameter | Standard |
Bulk density, g/cm³ | 0.70±0.10 |
Particle size, mm | 2.8±0.2 |
Strength factor, kg/mm, average, min. | 1.0 |
Space velocity, h-1 1-2
Temperature, °C 480-520
Pressure, MPa 2.5-3.5
Cycle length for production of reformate with RON 95-96 – 2 years
Catalyst life:
Warranted life – 5 years
Expected life – 8 years
Catalyst ensures the following:
- Regeneration cycle length of 12 months;
- Minimum catalyst life of 7 years run under severe conditions;
- High octane number
Manufactured according to Standard TU 20.59.56-31-44912618-2020
Composition:
Three grades of RU-135 catalyst are available – A, B and F with different content of platinum, rhenium and special promoters.
Catalysts of RU series are used in catalytic reforming process to increase the octane rating of naphtha and to produce BTX aromatics.
Specifications
Physical Properties | |||
---|---|---|---|
Standard | |||
Parameter | RU-135A | RU-135B | RU-135F |
Bulk density, g/cm³ | 0.64±0.02 | 0.64±0.02 | 0.70±0.05 |
Particle size, mm | 1.4±0.2 | 1.4±0.2 | 1.4±0.2 |
Strength factor, kg/mm, average, min. | 1.3 | 1.3 | 1.2 |
Process Conditions
Space velocity, h-1 1-2
Temperature, °C 470-520
Pressure, MPa 2.0-2.5
Catalyst ensures the following:
Production of reformate with RON 95-96 under severe conditions;
• Min. cycle length– 2 years;
• Total catalyst life (min.) – 10 years;
• Reformate yield – 86-88%
Manufactured according to Standard TU 2177-034-33160428-2009 Rev. 1
Composition:
Three grades of catalyst RB-44U are available, “A”, “B” and “Sh” with different content of platinum, rhenium and special promoters.
Catalyst RB-44U is designed for catalytic reforming process to produce high-octane gasoline components and C6-C8 aromatics.
Specifications
Physical Properties | |||
---|---|---|---|
Parameter | Standard | ||
A grade | B grade | Sh grade | |
Shape | Cylindrical extrudate | Cylindrical |
Spherical granule |
Bulk density, g/cm³ | 0.73-0.83 | 0.67-0.73 | 0.70-0.80 |
Particle size, mm | 1.4-1.8 | 1.2-1.6 | 1.6-2.0 |
Strength factor, kg/mm, min.
|
1.2 0.6 |
|
3.3 1.2 |
Recommended extrudate particle size for reactors with radial feed load - 1.6±0.2 mm, for reactors with axial feed load - 1.8±0.2 mm.
Process Conditions
Designed for fixed-bed units operated under low and medium pressure 1.2-2.5 MPa.
Expected regeneration cycle length of 2 years, run under severe conditions for RON 97-98; and 4 years for RON 95-96.
Manufactured according to Standard TU 2177-005-23092878-2000
Composition:
Two grades of catalyst RB-33U are available, “A” and “B” with different content of platinum, rhenium and special promoters.
Catalyst RB-33U is designed for catalytic reforming process to produce high-octane gasoline components and aromatics.
Specifications
Physical Properties | ||
---|---|---|
Parameter | Standard | |
A grade | B grade | |
Bulk density, g/cm³ | 0.75±0.05 | 0.72±0.03 |
Particle size, mm | 1.6±0.2 | 1.8±0.2 |
Strength factor, kg/mm, min. |
1.1 0.6 |
1.1 0.6 |
(Modified catalyst PK-P1)
Manufactured according to Standard TU 2177-014-44912618-01
Composition:
γ-alumina-supported platinum-rhenium with special promoters.
Catalyst TNK-23 is designed for naphtha reforming to produce gasoline components with RON 95-98 or aromatics.
Two grades of catalyst TNK-23 are available, “A” and “B”.
Specifications
Physical Properties | |
---|---|
Parameter | Standard |
Bulk density, g/cm³, не более | 0.7 |
Extrudate diameter, mm | 1.4±0.2 |
Strength factor, kg/mm, average, min. | 1.3 |