A kind of processing method of sour crude oil
A treatment method, a hydrogenation treatment technology, applied in the petroleum industry, refined hydrocarbon oil, etc., 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, and good reaction channels Effect
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Embodiment 1
[0055]Take by weighing silicon oxide content and be that the water glass 1000g of 30wt% adds in the beaker, start stirring device, slowly add mass concentration in the beaker and be the nitric acid solution 376g of 62%, make the pH value of water glass solution in the beaker be 2.0, add to above-mentioned Add 416.7g pseudo-boehmite in the solution (properties are as follows: pore volume 0.985mL / g, specific surface area is 313m 2 / g, the dry basis is 72wt%), after stirring evenly, add 83g of curing agent urea, add deionized water after the urea is completely dissolved, make the material in the beaker be a paste with certain fluidity, and use silicon dioxide and oxide The solids content based on aluminum was 33%.
[0056] Press the above paste material into the pre-prepared rigid body mold with spherical cavity and mandrel. After the paste material fills the entire cavity, insert the last short mandrel. When the short mandrel touches the first Fixed after the mandrel. Two vert...
Embodiment 2
[0060] The preparation process is as in Example 1, except that the mold is replaced, the diameter of the cavity and the mandrel is increased, and the prepared catalyst carrier B and catalyst B C The properties are shown in Table 1. Wherein, the outer diameter of the obtained catalyst carrier B is about 7.5 mm, and the diameter of the through holes is about 3.8 mm.
Embodiment 3
[0062] The preparation process is as in Example 1, except that 373g of nitric acid solution and 53g of nickel nitrate with a mass concentration of 62% will be slowly added to the beaker, and the solid content in terms of silicon dioxide and aluminum oxide is 35%, the prepared catalyst carrier C and Catalyst C C The properties are shown in Table 1. Wherein, the outer diameter of the obtained catalyst carrier C is about 5.5 mm, and the diameter of the through holes is about 2.5 mm.
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