A method for upgrading gasoline with high olefin content
A technology with high olefin content and high olefin, which is applied in the treatment of hydrocarbon oil, hydrocarbon oil treatment products, petroleum industry, etc. It can solve the problems of excessive oxygen in the blended gasoline and cannot be used in the factory, so as to increase the gasoline yield and improve the operating pressure. , the effect of reducing olefin content
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[0061] According to the present invention, the molecular sieve catalyst can use conventional catalysts well known to those skilled in the art, and the present invention has no special limitation thereto. In order to meet the operating requirements of fluidized bed reactors and regenerators, the shape of the molecular sieve catalyst is generally microsphere. The molecular sieve catalyst generally contains an active component and a support. According to a specific embodiment of the present invention, for example, wherein the molecular sieve catalyst may include an MFI type molecular sieve, a metal component, a carrier and a binder. Wherein the skeleton component of MFI type molecular sieve can be silicon, aluminum and / or phosphorus, and molecular sieve content can account for 10%-50% of catalyst gross weight; Metal component can be selected from zinc, iron, zirconium, gallium, silver, molybdenum At least one of metal components such as copper, nickel, manganese, chromium, plati...
Embodiment 1-4
[0081] Embodiment 1-4 takes the small molecule hydrocarbon compounds shown in Table 3 and the full cut stable gasoline shown in Table 2 as raw materials, and uses CRP-C catalyst to adopt figure 1 The process shown is for gasoline upgrading. The specific reaction conditions and reaction results are shown in Table 4. The regeneration temperature is 550°C, the regeneration pressure is 0.3MPa, the residence time of the catalyst is 12 minutes, and the fluidized medium is air.
Embodiment 5
[0083] Embodiment 5 takes the small molecular hydrocarbon compounds shown in Table 3 and the light gasoline shown in Table 2 as raw materials, and uses CRP-C catalyst to adopt figure 2 The process shown is for gasoline upgrading. The specific reaction conditions and reaction results are shown in Table 4. The regeneration temperature is 550°C, the regeneration pressure is 0.3MPa, the residence time of the catalyst is 12 minutes, and the fluidized medium is air.
[0084] As can be seen from Table 4, adopting the method of the present invention to carry out upgrading reaction to produce gasoline with low olefin content can not only isolate the hydrocarbon environment of the reaction and the oxygen environment of regeneration, and ensure the safety of the process, but also increase the reaction rate. pressure, increase the processing capacity of the device, and from the hydrocarbon composition and octane number of the gasoline obtained from the reaction, it can be seen that with t...
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