Combined process of hydrotreatment and catalytic cracking for residual oil
A hydrotreating and catalytic cracking technology, applied in hydrotreating process, petroleum industry, processing hydrocarbon oil, etc., can solve the problems of complex device, low conversion rate of fixed bed, complicated operation, etc., to reduce the difficulty of reaction and harsh processing. The effect of reducing the degree, type and number of devices, and improving the response effect
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Embodiment 1
[0032] In this embodiment, the combined process of fluidized bed, fixed bed and catalytic cracking in the hydrotreating of residue oil is used to carry out the hydroconversion of residue oil. Firstly, the residual oil raw material is preheated and then mixed with catalytic cracking heavy distillate oil and hydrogen into the ebullating bed hydroprocessing unit, and the hydrogenation reaction is carried out under the mixing and process conditions of different ebullating bed hydrogenation catalysts prepared to remove the hydrogenation in the raw material. Heteroatoms such as sulfur, nitrogen, and metals, while converting asphaltenes into colloids or smaller molecules, reducing product viscosity, hydrogenation products are separated to obtain liquid-phase modified oil, and the modified oil enters the fixed-bed hydrogenation unit The reaction is carried out, and the oil is obtained under the fixed-bed graded catalyst and reaction conditions. The resulting oil enters the catalytic c...
Embodiment 2
[0047] Compared with Example 1, the ebullated bed reactor uses a mixed catalyst. The long-term stability of the fixed bed is good, see Table 4 for details, and the temperature of the fixed bed reactor was increased by 3°C at 5000, 8000 and 12000 hours.
[0048] Table 5 Stability results of the fixed bed hydrogenation reaction system.
[0049] Example Example 1 Example 2 Operating time, hours Final oil metal content (μg / g) / total pressure drop of fixed bed reaction system (MPa) Final oil metal content (μg / g) / total pressure drop of fixed bed reaction system (MPa) 500 8.5 / 0.06 6.3 / 0.06 5000 8.7 / 0.08 6.8 / 0.06 8000 8.2 / 0.09 5.9 / 0.07 12000 9.1 / 0.11 6.5 / 0.08
[0050] As can be seen from the stability experiment results of the above-mentioned fixed bed reaction system, the method of the present invention can realize the long-term stable operation of the fixed bed hydrotreating unit, and it can be predicted according to the developm...
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