A catalytic cracking conversion method for increasing gasoline production and reducing oil slurry
A catalytic cracking and oil slurry technology, applied in the field of hydrocarbon catalytic cracking conversion, can solve the problems of difficult implementation, complex process, low gasoline yield, etc., and achieve the effects of ensuring uniform contact, improving average activity, increasing gasoline production and reducing gasoline production.
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Embodiment 1
[0052] use figure 1 The device shown and figure 2 The one-piece nozzle shown was tested.
[0053] The heights of light hydrocarbon reaction zone I, heavy oil reaction zone and light hydrocarbon reaction zone II account for 5%, 35% and 55% of the total height of the riser reactor respectively. The ratio of the outer diameter of the light hydrocarbon casing 20 of the integrated nozzle 12 to the outer diameter of the heavy hydrocarbon outer casing 19 is 2.20:1, and the diameter of a single light hydrocarbon injection hole on the light hydrocarbon nozzle 16 is the same as that of the single heavy hydrocarbon nozzle 18 on the heavy hydrocarbon outer nozzle. The aperture ratio of the hydrocarbon outer injection holes is 1.429:1. The pre-lift medium was nitrogen.
[0054] Residue hydrogenated diesel oil with a mass flow rate of 150g / h is sprayed from 4 light hydrocarbon nozzles 32 on the light hydrocarbon nozzle 16 of the integrated nozzle 12, in the light hydrocarbon reaction zo...
Embodiment 2
[0062] use figure 1 The device shown and figure 2 The one-piece nozzle shown was tested.
[0063] The heights of light hydrocarbon reaction zone I, heavy oil reaction zone and light hydrocarbon reaction zone II account for 5%, 35% and 55% of the total height of the riser reactor respectively. The ratio of the outer diameter of the light hydrocarbon casing 20 of the integrated nozzle 12 to the outer diameter of the heavy hydrocarbon outer casing 19 is 2.20:1, and the diameter of a single light hydrocarbon injection hole on the light hydrocarbon nozzle 16 is the same as that of the single heavy hydrocarbon nozzle 18 on the heavy hydrocarbon outer nozzle. The aperture ratio of the hydrocarbon outer injection holes is 1.429:1. The pre-lift medium was nitrogen.
[0064] Residue hydrogenated diesel oil with a mass flow rate of 150g / h is sprayed from 4 light hydrocarbon nozzles 32 on the light hydrocarbon nozzle 16 of the integrated nozzle 12, in the light hydrocarbon reaction zo...
Embodiment 3
[0071] use figure 1 The device shown and figure 2 The one-piece nozzle shown was tested.
[0072] The heights of light hydrocarbon reaction zone I, heavy oil reaction zone and light hydrocarbon reaction zone II account for 5%, 35% and 55% of the total height of the riser reactor respectively. The ratio of the outer diameter of the light hydrocarbon casing 20 of the integrated nozzle 12 to the outer diameter of the heavy hydrocarbon outer casing 19 is 2.20:1, and the diameter of a single light hydrocarbon injection hole on the light hydrocarbon nozzle 16 is the same as that of the single heavy hydrocarbon nozzle 18 on the heavy hydrocarbon outer nozzle. The aperture ratio of the hydrocarbon outer injection holes is 1.429:1. The pre-lift medium was nitrogen.
[0073] Residue hydrogenated diesel oil with a mass flow rate of 150g / h is sprayed from 4 light hydrocarbon nozzles 32 on the light hydrocarbon nozzle 16 of the integrated nozzle 12, in the light hydrocarbon reaction zo...
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