Oil-soluble molybdenum caprylate catalyst as well as preparation method and application thereof
A catalyst and oil-soluble technology, which is applied in the field of preparation of oil-soluble molybdenum octoate catalyst, can solve the problems of low metal content, high storage requirements, external vulcanization and other problems, and achieves the effects of low solid content, good dispersion effect and convenient operation.
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[0030] Example 1
[0031] An oil-soluble octano-molybdenum catalyst provided by this example and the preparation method thereof, including the following steps:
[0032] 1) A mixture of molybdated acid, acetic anhydride, and isotoic acid in molar ratio of 1: 2: 4, and mix well by electromagnetic stirrer to obtain a mixture;
[0033] 2) Under stirring, the mixture is heated to 70 ° C, and the reaction is 1 h;
[0034] 3) Heating under vacuum, removes the acetic acid of the sub-reactive product;
[0035] 4) Heating to 150 ° C continued to react 2 h, and the oil-soluble hydrothermolybdenum catalyst can be obtained after the reaction.
Example Embodiment
[0036] Example 2
[0037] An oil-soluble octano-molybdenum catalyst provided by this example and the preparation method thereof, including the following steps:
[0038] 1) Ammonium molybdenate, acetic anhydride, isochinic acid, to ensure molybdenum atom, acetic anhydride, and isteric acid in molar ratio 1: 3: 5, mix well by electromagnetic stirrer, resulting in a mixture;
[0039] 2) Under the action of stirring, heating the mixture to 80 ° C, reacting 1.5 h;
[0040] 3) Heating under vacuum, removes the acetic acid of the sub-reactive product;
[0041] 4) Heating to 160 ° C continued to react 2H, and the oil-soluble hydrothermolybdenum catalyst can be obtained after the reaction.
Example Embodiment
[0042] Example 3
[0043] The catalyst prepared in the above examples is used in the hydrocracking reaction of the Middle Eastern reducing residue, and the MO / NI compound catalyst prepared by the metal Ni is added (MO: Ni = 1: 1) in the same conditions. Next, the reaction temperature is 432 ° C, the reaction pressure is 12 MPa, the reaction time is 60 min, and the catalyst is 150 ppm (in the active metal total meter), the material properties are shown in Table 1, the test product distribution is shown in Table 2:
[0044] Table 1, raw material oil properties
[0045] Analysis Project Middle East reduction Density (20 ° C), g / cm3 1.03 S content, wt% 5.1 N content, WPPM 5420 WT% 21.6 Ni content, WPPM 65 V content, WPPM 212
[0046] Table 2, Test Product Distribution
[0047]
[0048] It can be seen from Table 2, which is obviously improved by the addition of the catalyst after the addition of the catalyst, in particular, examples 1 a...
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