Vulcanization method of selective hydrodesulfurization catalyst of FCC (Fluid Catalytic Cracking) gasoline
A hydrodesulfurization and selectivity technology, applied in catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc. In order to achieve the effect of maintaining selectivity, reducing octane number loss, and enhancing the active center of desulfurization
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Embodiment 1
[0034] Catalyst SHD-1 is selected as the FCC gasoline selective hydrogenation catalyst, the vulcanizing agent is dimethyl disulfide, the vulcanization conditions and process are as follows: the system pressure is 1.8MPa, after passing the airtight inspection, the reactor inlet is raised to 140°C , and then start the feed pump to feed the vulcanized oil, the liquid hourly volume space velocity is 2h -1 . The concentration of dimethyl disulfide in vulcanized oil is 4wt%. After 4 hours of constant temperature, the temperature is raised to 230°C at a rate of 15°C / h. After the temperature rises to 230°C, the temperature is kept constant. 2 After S penetrates the bed, keep the temperature constant for 8 hours. Then adjust the system pressure to 4.5MPa, then raise the temperature to 290°C at a rate of 15°C / h, and keep the temperature constant for 10 hours after the temperature rises to 290°C. After the sulfidation process of the catalyst is completed, the system pressure is reduced...
Embodiment 2
[0040] Catalyst SHD-2 is selected as the FCC gasoline selective hydrogenation catalyst, the system pressure of the low-temperature vulcanization section is 1.6MPa, other process conditions are consistent with embodiment 1, and the process conditions of the high-temperature vulcanization section are: the system pressure is changed to 4.0MPa, and the vulcanization temperature is 300 DEG C, all the other are consistent with embodiment 1.
[0041] The conditions of the FCC gasoline selective desulfurization process test also remain consistent with that of Example 1, and the results are shown in attached table 3.
Embodiment 3
[0046] Catalyst SHD-3 is selected as the FCC gasoline selective hydrogenation catalyst, the process conditions of the low-temperature vulcanization section are consistent with those in Example 1, and the process conditions of the high-temperature vulcanization section are: the system pressure is changed to 5.0 MPa, the vulcanization temperature is 310°C, and the rest are the same as those in Example 1. 1 is consistent.
[0047] The conditions of the FCC gasoline selective desulfurization process test also remain consistent with that of Example 1, and the results are shown in attached table 3.
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