Processing method before applying hydrogenation catalyst
A technology for hydrogenation catalysts and treatment methods, applied in chemical instruments and methods, catalyst activation/preparation, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of reducing catalyst self-heating and not completely solving the problem of sulfided catalysts Self-heating problem and other problems, to achieve the effect of improving vulcanization effect, reducing sulfur loss, and improving performance
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Embodiment 1
[0025] 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.
[0026] The specific pre-sulfurization process is as follows:
[0027] 1. The molten elemental sulfur is introduced into the oxidation state catalyst, and the amount of elemental sulfur introduced is 105% of the theoretical sulfur requirement of the catalyst. It was then impregnated with a coker diesel fraction in an amount of 45% by weight of the catalyst.
[0028] 2. The catalyst obtained in step 1 was treated under normal pressure and in the presence of water vapor at 160°C for 7 hours, the temperature of the water vapor introduced was 110°C, and 1kg of steam was passed per 100kg of catalyst to obtain the final hydrorefining catalyst containing sulfiding agent EPRES-1.
Embodiment 2
[0030] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.
[0031] The specific pre-sulfurization process is as follows:
[0032] 1. Uniformly impregnate triethylamine on the oxidized FH-5A catalyst, and the addition amount of triethylamine is 5% of the catalyst weight to obtain a catalyst loaded with triethylamine.
[0033] 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 15% of the catalyst weight, and the amount of elemental sulfur is 105% of the theoretical sulfur content of the catalyst containing metal. The catalyst loaded with triethylamine obtained in step 1 was spray-impregnated with a solvent of elemental sulfur.
[0034] 3. The catalyst obtained in step 2 is treated at 160°C for 2 hours under normal pressure and in the presence of water vapor, and then treated at 230°C for 4 hours. Hydrofining catalyst EPRES-2.
Embodiment 3
[0038] The catalyst in the oxidation state is the same as in Example 1, which is FH-5A.
[0039] The specific pre-sulfurization process is as follows:
[0040] 1. Dissolve triethylamine and gluconic acid in 4:1 by weight ratio in ammonia water containing 8wt% ammonia, impregnate the oxidized catalyst with the solution, the amount of the above substances is 15% of the catalyst weight, and then dry at 130°C for 4 hours, a catalyst containing mixed organic additives was obtained.
[0041] 2, vacuum distillate oil and peanut oil volume ratio are 1: 2 miscible solvent, solvent consumption is 0.5% of catalyst weight, then mixes with elemental sulfur solid powder, and elemental sulfur consumption is 90% of catalyst metal-containing theoretical sulfur requirement.
[0042] 3. The material obtained in step 2 is treated at 110°C for 15 hours and at 160°C for 10 hours under normal pressure and in the presence of water vapor. Hydrofining catalyst EPRES-3.
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