System and method for catalyzing hydrocarbon for recombinant production of high-quality gasoline
A high-quality, heavy gasoline technology, used in gasoline stabilization, refined hydrocarbon oil, petroleum industry, etc., to achieve the effect of low sulfur content and low olefin content
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0035] Such as Picture 1-1 Shown is a schematic flow chart of one of the embodiments of the present invention. The distillation range is 30-205°C, the sulfur content is 100ppm, the mercaptan content is 5ppm, the olefin content is 30% (v), the diene content is 0.1% (v), the aromatic content is 15% (v), octane The alkane number (RON) is 89 and the density is 728 kg / m 3 The stable gasoline (catalyzed gasoline) is first hydrotreated in the hydrogenation unit 3-1 with a flow rate of 100,000 tons / year, and the catalyst in the hydrogenation unit 3-1 is a selective hydrogenation catalyst GHT-20; The volume space velocity ratio of the hydrogenation unit 3-1 is 2; the hydrogen / oil volume ratio is 150; the operating temperature is 230° C., and the operating pressure is 0.6 MPa (absolute); The tower top temperature of tower 1 is 82 ℃, and tower bottom temperature is 190 ℃, and tower top pressure is 0.2MPa (absolute), and tower bottom pressure is 0.25MPa (absolute), fractionation obtai...
Embodiment 2
[0056] Such as Figure 1-2 Shown is a schematic flow chart of Embodiment 2 of the present invention. The distillation range is 30-205°C, the sulfur content is 2000ppm, the mercaptan content is 50ppm, the olefin content is 40% (v), the diene content is 1.0% (v), the aromatic content is 19% (v), octane The alkane number (RON) is 91 and the density is 728 kg / m 3 The stable gasoline (catalyzed gasoline) is first hydrotreated in the hydrogenation unit 3-1 with a flow rate of 100,000 tons / year, and the catalyst in the hydrogenation unit 3-1 is a selective hydrogenation catalyst GHT-20; The volume space velocity ratio of the hydrogenation unit 3-1 is 3; the hydrogen / oil volume ratio is 200; the operating temperature is 240° C., and the operating pressure is 1.0 MPa (absolute); The tower top temperature of tower 1 is 86 ℃, and tower bottom temperature is 192 ℃, and tower top pressure is 0.2MPa (absolute), and tower bottom pressure is 0.25MPa (absolute), fractionation obtains light ...
Embodiment 3
[0060] Such as Figure 1-2 Shown is a schematic flow chart of the third embodiment of the present invention. The distillation range is 30-205°C, the sulfur content is 2000ppm, the mercaptan content is 50ppm, the olefin content is 40% (v), the diene content is 1.0% (v), the aromatic content is 19% (v), octane The alkane number (RON) is 91 and the density is 728 kg / m 3 The stable gasoline (catalyzed gasoline) is first hydrotreated in the hydrogenation unit 3-1 with a flow rate of 100,000 tons / year, and the catalyst in the hydrogenation unit 3-1 is a selective hydrogenation catalyst GHT-20; The volume space velocity ratio of the hydrogenation unit 3-1 is 3; the hydrogen / oil volume ratio is 200; the operating temperature is 240° C., and the operating pressure is 1.0 MPa (absolute); The tower top temperature of tower 1 is 86 ℃, and tower bottom temperature is 192 ℃, and tower top pressure is 0.2MPa (absolute), and tower bottom pressure is 0.25MPa (absolute), fractionation obtain...
PUM
| Property | Measurement | Unit |
|---|---|---|
| density | aaaaa | aaaaa |
| density | aaaaa | aaaaa |
| density | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 