Hydrocarbon hydroprocessing technique
A technology for hydrotreating and process method, which is applied in refining to remove heteroatoms and other directions, can solve the problems of unfavorable hydrotreating process, can not completely solve the problem of self-heating of sulfurized catalyst, low catalyst production efficiency, etc., so as to shorten the sulfurization time. , suitable for large-scale use, the effect of improving the vulcanization effect
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Embodiment 1
[0035] The commercial hydrodesulfurization catalyst FH-5A (developed by Fushun Petrochemical Research Institute and produced by Wenzhou Huahua Group Co., Ltd.) was selected. The main composition and properties are shown in Table 1.
[0036] The specific pre-sulfurization process is as follows:
[0037] 1. Dissolve tetrabutylthiuram disulfide (TBTD) in benzene, evenly impregnate it on the oxidized FH-5A catalyst, and then treat it at 100°C for 3 hours to remove benzene. The TMTD addition is 3% of the catalyst weight, A catalyst supporting TMTD was obtained.
[0038] 2. Introducing molten elemental sulfur into the catalyst obtained in step 1, the amount of elemental sulfur introduced is 105% of the theoretical sulfur requirement of the catalyst. Coked diesel is then introduced in an amount of 40% by weight of the catalyst. Finally, it was treated at 160° C. for 5 hours under normal pressure and in a stagnant air atmosphere to obtain the hydrorefining catalyst EPRES-1 finally c...
Embodiment 2
[0040] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.
[0041] The specific pre-sulfurization process is as follows:
[0042] 1. Dissolve tetramethylthiuram disulfide (TMTD) in benzene, evenly impregnate it on the oxidized FH-5A catalyst, and then evaporate and remove benzene at 100°C. The amount of TMTD added is 5% of the weight of the catalyst , to obtain a catalyst loaded with TMTD.
[0043] 2. Dispersing the elemental sulfur in a solvent with a volume ratio of catalytic cracking gasoline and rapeseed oil of 8:1, the amount of solvent is 12% of the catalyst weight, and the amount of elemental sulfur is 90% of the metal-containing theoretical sulfur required by the catalyst. The catalyst loaded with TMTD obtained in step 1 was impregnated in a solvent of elemental sulfur, and finally treated at 140° C. for 2 hours under nitrogen. The final hydrorefining catalyst EPRES-2 containing a sulfurizing agent was obtained.
Embodiment 3
[0047] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.
[0048] The specific pre-sulfurization process is as follows:
[0049] 1. Dissolve dithiodimethyldiphenylthiuram in acetone and introduce it into the catalyst in an oxidized state. The amount of dithiodimethyldiphenylthiuram is 20% of the catalyst weight, and then at 105°C Under treatment for 3 hours, a catalyst containing dithiodimethyldiphenylthiuram was obtained.
[0050] 2, vacuum distillate oil and peanut oil volume ratio are the miscible solvent of 1: 2, solvent consumption is 0.5% of catalyst weight, then mixes with elemental sulfur solid powder, elemental sulfur consumption is 40% of catalyzer metal-containing theoretical sulfur demand.
[0051] 3. The material obtained in step 2 was treated at 180° C. for 3 hours under normal pressure and in a stagnant air atmosphere to obtain a hydrorefining catalyst EPRES-3 finally containing a vulcanizing agent.
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