A catalytic conversion method for producing clean gasoline from inferior raw material oil
A catalytic conversion method and low-quality raw material oil technology, which is applied in the direction of catalytic cracking, cracking, and hydrocarbon oil treatment, can solve the problems of reducing the effective reaction area of molecular sieves, reducing the reaction activity of molecular sieves, and reducing reaction selectivity. The effect of improving yield and conversion rate
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Embodiment 1
[0082] This example follows figure 1 The process of the test is carried out, and the vacuum residue A is used as the inferior raw material oil, in the medium-sized device of the riser reactor (the height of the riser reactor 2 is 30 meters, the inner diameter of the pre-lift section is 0.8 meters, and the height of the pre-lift section is 1.5 meters. m, the inner diameter of the first reaction section I is 1 meter, the height of the first reaction section I is 6 meters, the inner diameter of the first expansion section III is 3 meters, the height of the expansion section III is 1 meter, and the second reaction section II Inner diameter is 1 meter, and the height of the second reaction section II is 19 meters, and the inner diameter of outlet section 7 is 0.8 meters, and the height of outlet section 7 is 2.5 meters, the same below) carries out test, and catalyst used is the catalyst prepared by the present invention a. The vacuum residue A enters the lower part of the first re...
Embodiment 2
[0091] This example follows figure 2The flow process of the present embodiment is tested in the medium-sized device of the riser reactor (the height of the riser reactor 2 is 30 meters, the inner diameter of the pre-lift section is 0.8 meters, the height of the pre-lift section is 1.5 meters, the first reaction section 1 The inner diameter is 1 meter, the height of the first reaction section I is 6 meters, the inner diameter of the first expanding section III is 3 meters, the height of the first expanding section III is 1.5 meters, the inner diameter of the reducing section is 1 meter, and the height is 1 meter, the inner diameter of the second diameter expansion section III' is 3 meters, the height of the second diameter expansion section III' is 1.5 meters, the inner diameter of the second reaction section II is 0.8 meters, and the height of the second reaction section II is 17.5 meters M) on test, catalyst used is catalyst A prepared by the present invention. The coker wa...
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