Method for modifying poor gasoline
A low-quality gasoline and gasoline technology, applied in the petroleum industry, refined hydrocarbon oil, etc., can solve the problems of reforming catalyst movement, complicated regeneration process, and the inability to reduce olefin content and aromatic content, so as to reduce sulfur content and octane number without loss or added effect
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Embodiment 1
[0040] In this embodiment, only FCC gasoline is used as the reaction raw material, and no alkylating agent is added to the raw material. The catalyst used is composed of 60% by weight of HZSM-5 molecular sieve (the ratio of silicon to aluminum is 120) and the rest of the pseudo-boehmite carrier. . The FCC gasoline upgrading experiment was carried out on a small fixed bed device. The reaction conditions were: reaction temperature 360°C, reaction pressure 1.0MPa, weight space velocity 1.0h -1 . The reaction results are listed in Table 3. As can be seen from Table 3, the sulfur content in the gasoline product is 191.4ppm.
Embodiment 2
[0042] Compared with Example 1, in this example, an alkylating agent, that is, FCC liquefied gas, is added to the raw material, and the weight ratio of FCC liquefied gas to low-quality gasoline raw material is 0.083:1, and other conditions are the same as in Example 1. The reaction results are listed in Table 3. As can be seen from Table 3, the sulfur content in the gasoline product is reduced to 149.0ppm.
Embodiment 3
[0044] This example illustrates that the method provided by the present invention can deeply remove sulfur in FCC gasoline.
[0045] The weight ratio of FCC gasoline raw material to FCC liquefied gas as an alkylating agent is 12:1, and the catalyst is composed of 60% by weight of HZSM-5 zeolite (silicon-aluminum ratio of 30) and the balance of pseudo-boehmite carrier. The FCC gasoline upgrading experiment was carried out on a small fixed bed device. The reaction conditions were: reaction temperature 360°C, reaction pressure 1.0MPa, weight space velocity 1.0h -1 , the agent-to-oil ratio is 1. The reaction results are listed in Table 4. As can be seen from Table 4, the sulfur content in the gasoline product is only 11.4ppm, which can almost transfer all the thiophene sulfides in the raw material to the diesel fraction; at the same time, the olefins in the gasoline are significantly reduced to 10ppm. Below the weight %, the octane number increases obviously.
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