Depth hydrogenation treatment method of faulty gasoline
A low-quality gasoline and deep hydrogenation technology, which is applied in the combined process of upgrading and olefin reduction, and in the field of deep desulfurization of catalytic cracked gasoline, can solve the problems of octane number loss and increased hydrogen consumption, and achieve high desulfurization activity and selectivity. Operation process, avoiding the effect of high hydrogen consumption
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preparation example Construction
[0015] The preparation method of the hydrodesulfurization catalyst is any conventional impregnation method. The oxide can be impregnated step by step, preferably co-impregnation; the impregnating solution can be impregnated with the same adsorption amount, or the impregnating solution can be impregnated excessively.
[0016] The aromatization and hydrodesulfurization provided by the invention are carried out in the same high-temperature reactor. The reaction pressure is generally 1.5MPa~4.5MPa, the reaction temperature is generally 360℃~460℃, and the total volume space velocity is generally 1.0h -1 ~5.0h -1 , the volume ratio of hydrogen to oil is generally 200:1~1000:1; the reaction pressure is preferably 2.5MPa~3.5MPa, the reaction temperature is preferably 380°C~420°C, and the total volume space velocity is preferably 2.0h -1 ~4.0h -1 , the volume ratio of hydrogen to oil is preferably 500-700:1.
[0017] Because the temperature of the product at the outlet of the secon...
example 1
[0020] This example is a combined process of selective hydrofinishing / upgrading (aromatization) and hydrodesulfurization.
[0021] The experiment was carried out on a device with two reactors connected in series, the first reactor was filled with MoO 3(12.0wt%)-CoO(4.5wt%) / Al 2 o 3 Selective hydrofinishing catalyst; second reactor charged with a La 2 o 3 -NiO-ZnO / HZSM-5+HBeta aromatization catalyst, the catalyst La 2 o 3 1.0wt%, NiO 2.6wt%, ZnO 1.5wt%, HZSM-5 grain size 20nm ~ 80nm (SiO 2 / Al 2 o 3 Molar ratio 27) content is 35wt%, HBeta grain size is 80nm~150nm (SiO 2 / Al 2 o 3 Molar ratio 33) content is 40wt%. Hydrodesulfurization catalyst is MoO 3 (3.0 wt%)-CoO(1.0 wt%)-ZnO(1.0 wt%) / alumina. The volume ratio of the aromatization catalyst to the hydrodesulfurization catalyst is 15:1. First, pre-sulfurize the catalyst, the vulcanized oil is straight-run gasoline, and the vulcanizing agent is CS 2 , CS 2 The concentration is 1.0v%; the vulcanization pressure is...
Embodiment 2
[0025] Change the hydrodesulfurization catalyst in embodiment 1 into MoO 3 (4.0wt%)-CoO(1.0wt%)-CuO(1.0wt%) / alumina catalyst, the volume ratio of the aromatization modification catalyst is 20:1, the average temperature of the second reactor is 400°C, Others are with embodiment 1. The specific results of the reaction for 500 hours are shown in Table 2.
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