Hydrocarbon oil catalytic conversion method of a light hydrocarbon and heavy hydrocarbon composite raw material
A catalytic conversion method and catalytic cracking technology are applied in the field of catalytic conversion for improving the yield of gasoline and propylene, and can solve the problems of low gasoline yield, high propylene yield, complicated process, etc., and achieve accelerated cracking of heavy hydrocarbons, increased gasoline production, The effect of even contact
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Embodiment 1
[0050] according to figure 1 The device shown and figure 2 The one-piece nozzle shown was tested.
[0051] The heights of light hydrocarbon reaction zone I, heavy hydrocarbon 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 to the outer diameter of the heavy hydrocarbon outer casing is 2.20:1, and the ratio of the aperture diameter of a single light hydrocarbon nozzle on the light hydrocarbon nozzle to the diameter of a single heavy hydrocarbon outer nozzle on the heavy hydrocarbon nozzle is 1.429:1. The pre-lift medium was nitrogen.
[0052] 3 million catalytically cracked naphtha with a mass flow rate of 150 g / h is sprayed from 4 light hydrocarbon nozzles 31 on the light hydrocarbon nozzle 15 of the integrated nozzle 11, and is injected into the light hydrocarbon reaction zone I in the riser reactor 4 and regenerated Cata...
Embodiment 2
[0057] according to figure 1 The device shown and figure 2 The one-piece nozzle shown was tested.
[0058] The heights of light hydrocarbon reaction zone I, heavy hydrocarbon 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 to the outer diameter of the heavy hydrocarbon outer casing is 2.20:1, and the ratio of the aperture diameter of a single light hydrocarbon nozzle on the light hydrocarbon nozzle to the diameter of a single heavy hydrocarbon outer nozzle on the heavy hydrocarbon nozzle is 1.429:1. The pre-lift medium was nitrogen.
[0059] 3 million catalytically cracked naphtha with a mass flow rate of 150 g / h is sprayed from 4 light hydrocarbon nozzles 31 on the light hydrocarbon nozzle 15 of the integrated nozzle 11, and is injected into the light hydrocarbon reaction zone I in the riser reactor 4 and regenerated Cata...
Embodiment 3
[0064] according to figure 1 The device shown and figure 2 The one-piece nozzle shown was tested.
[0065] The heights of light hydrocarbon reaction zone I, heavy hydrocarbon 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 to the outer diameter of the heavy hydrocarbon outer casing is 2.20:1, and the ratio of the aperture diameter of a single light hydrocarbon nozzle on the light hydrocarbon nozzle to the diameter of a single heavy hydrocarbon outer nozzle on the heavy hydrocarbon nozzle is 1.429:1. The pre-lift medium was nitrogen.
[0066] 3 million catalytically cracked naphtha with a mass flow rate of 150 g / h is sprayed from 4 light hydrocarbon nozzles 31 on the light hydrocarbon nozzle 15 of the integrated nozzle 11, and is injected into the light hydrocarbon reaction zone I in the riser reactor 4 and regenerated Cata...
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