High efficiency catalytic conversion method of petroleum hydrocarbon
A catalytic conversion method and technology of petroleum hydrocarbons, applied in the field of catalytic conversion of integrated processes, can solve problems such as low sulfur content, difficulty in maintaining balanced operation, and reduced processing efficiency
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Embodiment 1
[0080] This example illustrates the product distribution and product properties of raw material A after being treated by a medium-sized catalytic cracking unit and a medium-sized hydrotreating unit using the method provided by the present invention.
[0081] The preheated raw material A is first processed in a medium-sized catalytic cracking unit. The total height of the pre-lifting section, the first reaction zone, the second reaction zone, and the outlet zone of the reactor of the medium-sized catalytic cracking unit is 15 meters, and the diameter of the pre-lifting section is 0.025 meters, its height is 1.5 meters; the diameter of the first reaction zone is 0.025 meters, its height is 4 meters; the diameter of the second reaction zone is 0.1 meters, its height is 6.5 meters; the diameter of the outlet zone is 0.025 meters, its height is 3 meters m; the vertex angle of the isosceles trapezoid in the longitudinal section of the joint of the first and second reaction zones is 4...
Embodiment 2
[0087] This example illustrates the product distribution and product properties of raw material B treated by a medium-sized catalytic cracking unit and a medium-sized hydrotreating unit using the method provided by the present invention.
[0088] The preheated raw material B is first processed in a medium-sized catalytic cracking unit. The total height of the pre-lifting section, the first reaction zone, the second reaction zone, and the outlet zone of the reactor of the medium-sized catalytic cracking unit is 15 meters, and the diameter of the pre-lifting section is 0.025 meters, its height is 1.5 meters; the diameter of the first reaction zone is 0.025 meters, its height is 4 meters; the diameter of the second reaction zone is 0.1 meters, its height is 6.5 meters; the diameter of the outlet zone is 0.025 meters, its height is 3 meters m; the vertex angle of the isosceles trapezoid in the longitudinal section of the joint of the first and second reaction zones is 45°; the base...
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