Hydro-cracking method for blending ethylene bottom oil
A technology of ethylene tar refining and hydrocracking, which is applied in the field of hydrocracking of vacuum gas oil blended with ethylene tar to produce light fuel oil, can solve the problems of ineffective treatment and inability to process ethylene tar fractions, and achieve expansion Raw material sources, increased saturation rate, and even effects of exothermic reaction
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Embodiment 1~3
[0035] The properties of the ethylene tar light fraction and VGO raw materials used are shown in Table 2.
[0036] The hydrogenation protection catalyst used in this example is FZC-103, and the hydrogenation refining catalyst used is 3936. This embodiment adopts a series hydrogenation process, two reactors, the first reactor is filled with a hydrogenation protection catalyst and a hydrofining catalyst, and the second reactor is filled with a hydrogenation carbon removal catalyst and a hydrocracking catalyst. The operating conditions and reaction results used are shown in Table 3.
Embodiment 4
[0048] The heavy fraction of ethylene tar is heat-treated at 380°C under normal pressure for 20 minutes to obtain mesophase pitch; the mesophase pitch is melt-spun with a pneumatic spinning machine, and the spun pitch fiber is oxidized by air at 300°C-400°C to form The fibers were not melted, and then carbonized into carbon fibers at 1000°C under nitrogen. The properties of the obtained pitch-based carbon fibers are shown in Table 5.
[0049] Table 4 Properties of Ethylene Tar Heavy Fraction
[0050] crude oil name
Ethylene tar heavy fraction (>430°C)
carbon to hydrogen ratio
1.07
[0051] crude oil name
Ethylene tar heavy fraction (>430°C)
Softening point / ℃
225
Quinoline insoluble matter / %
0.60
[0052] Table 5 Properties of pitch-based carbon fibers
[0053] project
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