A kind of hydrotreating method of sour crude oil
A technology for hydroprocessing and crude oil, which is applied in the fields of hydroprocessing process, hydrocarbon oil treatment, petroleum industry, etc. It can solve the problems of cumbersome loading and unloading of different types, catalyst back-mixing, etc., and achieve long operation period of the device, high hydrogenation activity, The effect of a good response channel
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Embodiment 1
[0059] Take by weighing 400 g of water glass with a silicon oxide content of 30 wt % and add it to the beaker, start the stirring device, slowly add 150 g of nitric acid solution with a mass concentration of 62% in the beaker, then add 42.9 g of nickel nitrate, stir and dissolve the water glass solution in the beaker The pH value is 2.0, then add 385.3g pseudo-boehmite (properties are as follows: pore volume 1.05mL / g, specific surface area is 306m 2 / g, dry basis is 70wt%), after stirring evenly, add curing agent urea 35g, add deionized water after the urea is all dissolved, make the material in the beaker be the paste with certain fluidity, and with silicon dioxide and oxide The solids content based on aluminum was 33%.
[0060] The above paste mass is pressed into two identical hemispheres with spherical cavities. Wherein, a guide mold is placed in a hemisphere, and the guide mold is made of wood. The structure of the guided mode is that there is a cylinder in the x-axis, ...
Embodiment 2
[0065] The preparation process is as in Example 1, except that the solid content of silica and alumina is 35%, and the mold is replaced, the diameter of the cavity and cylinder is increased, and the prepared catalyst carrier B and catalyst B C , whose properties are shown in Table 1. Wherein, the outer diameter of the obtained catalyst carrier B is about 9.5 mm, the diameter of the middle through hole is about 3.0 mm, and the diameter of the side through hole is about 1.6 mm.
Embodiment 3
[0067] The preparation process is as in Example 1, except that nickel nitrate is not added, the prepared catalyst carrier C and catalyst C C , whose properties are shown in Table 1. Wherein, the outer diameter of the obtained catalyst carrier C is about 7.0 mm, the diameter of the middle through hole is about 1.9 mm, and the diameter of the side through hole is about 1.3 mm.
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