Hydrotreating method for heavy hydrocarbon raw material by adopting up-flow reactor
A hydrotreating and reactor technology, applied in the treatment of hydrocarbon oil, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of catalyst bed disturbance, accelerated deactivation, easy to cause hot spots, etc.
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Embodiment 1
[0063] Taking by weighing silicon oxide content is the water glass 1071g of 28wt% and adds in the beaker, start stirring device, slowly add mass concentration in the beaker and be the nitric acid solution 370g of 65%, the pH value of water glass solution in the beaker after stirring and dissolving is 2.0, then Add 93.14g of nickel nitrate hexahydrate, dissolve and then add 585g of aluminum sol (the properties are as follows: the Al / Cl ratio is 1.40, the alumina content is 28wt%) and γ-Al 2 o 3 163.8g (the properties are as follows: the pore volume is 1.098mL / g, the specific surface area is 302m 2 / g), stir well and then add curing agent 93.6g hexamethylenetetramine, add deionized water after the hexamethylenetetramine is completely dissolved, so that the material in the beaker is a paste with certain fluidity, and The solids content based on silica and alumina was 33%.
[0064] The above paste mass is pressed into two identical hemispheres with spherical cavities. Wherein, ...
Embodiment 2
[0068] The preparation process is as in Example 1, except that the curing agent hexamethylenetetramine is changed to add 97.2g urea, the amount of nickel nitrate hexahydrate is changed to add 62.5g, and the prepared catalyst carrier B and catalyst B C The properties are shown in Table 1.
[0069] Wherein, the outer diameter of the catalyst carrier B obtained is about 9.5mm, the through-hole diameter of the first passage, the second passage and the third passage is about 2.6mm, and the length of the first passage, the second passage and the third passage is 9.5mm ; The lengths of the fourth channel, the fifth channel, the sixth channel and the seventh channel forming the square channel are all 7.2 mm, and the channel diameter is about 1.4 mm.
Embodiment 3
[0071] The preparation process is as in Example 1, except that the mold is replaced, the diameter of the cavity and the cylinder is increased, and the prepared catalyst carrier C and catalyst C C The properties are shown in Table 1.
[0072] Wherein, the outer diameter of gained catalyst carrier C is about 7.5mm, and the through hole diameter of the first passage, the second passage and the third passage is about 2.6mm, and the length of the first passage, the second passage and the third passage is 7.5mm , the lengths of the fourth channel, the fifth channel, the sixth channel and the seventh channel forming the square channel are all 6 mm, and the channel diameter is about 1.3 mm.
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