Device and method for producing clean gasoline by combining catalytic cracking and hydrofining
A hydrorefining and catalytic cracking technology, which is applied in the fields of hydrotreating process, petroleum industry, and hydrocarbon oil treatment, etc., can solve problems that are not involved, increase energy consumption and equipment investment, and not involve catalytic cracking and hydrofining systems Coupling and other issues
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Embodiment 1
[0065] Embodiment 1: Two-stage riser reactor
[0066] like figure 1 As shown, the device for the combined production of clean gasoline by catalytic cracking and hydrofinishing provided in this example includes a reaction-regeneration system, a fractionation system, a hydrofinishing unit and an absorption-stabilization system,
[0067] Among them, the reaction-regeneration system includes a riser reactor, an oil separator and a catalyst regenerator,
[0068] The riser reactor is a two-stage riser reactor, comprising a first riser reactor 10 and a second riser reactor 11, the upper end of the first riser reactor 10 communicates with the oil separator 12, and the second riser reactor The upper end of the tube reactor 11 communicates with the oil separator 12, and the first riser reactor 10 is provided with a pre-lift gas inlet 103, a catalyst feed port 102 and a feedstock oil feed port 101 from bottom to top, and the second riser reactor The device 11 is provided with a pre-lif...
Embodiment 2
[0080] The device of the present invention see figure 2 , its structure is basically the same as that of Example 1, except that the second riser reactor adopts a combination reactor of a fast bed and a transport bed. like figure 2 As shown, the second riser reactor is composed of the pre-lift section, the transport bed reaction zone and the fast bed reaction zone from bottom to top. The specific design requirements are as follows: the total height of the reactor is 30~60m; 5%~20% of the height, the height of the transport bed reaction zone accounts for 30~60% of the total height of the reactor, and its diameter is 1.0~2.0 times the diameter of the pre-lifting section; the height of the fast bed reaction zone accounts for 20% of the height of the riser reactor ~50%, its diameter is 1.5~5.0 times of the diameter of the conveying bed reaction zone; among them, the pre-lifting section is provided with pre-lifting gas inlet 114 and catalyst feed port 113 from bottom to top, and ...
Embodiment 3
[0082] Embodiment 3: single-stage riser reactor
[0083] like image 3 As shown, the device for the joint production of clean gasoline by catalytic cracking and hydrofining provided in this example is similar to Example 1, except that the riser reactor of the reaction regeneration system in this example is a single-stage riser reactor.
[0084] Knot image 3 , the difference between the two devices is described as follows:
[0085] The upper end of the riser reactor 11' communicates with the oil separator 12', and the riser reactor 11' is provided with a pre-lift gas inlet 114', a catalyst feed port 113', a raw oil feed port 101', Circulating oil feed port 111' and naphtha light fraction feed port 112', the solid phase outlet of the oil separator 12' communicates with the catalyst regenerator 13, and the catalyst regenerator 13 communicates with the catalyst of the riser reactor 11' through pipelines. The feeding port 113' is connected;
[0086] The oil separator 12' inclu...
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