Method for improving stable operation of hydrocracking unit
A hydrocracking and stable operation technology, which is applied in the fields of hydroprocessing process, petroleum industry, and hydrocarbon oil treatment, can solve the problems of hydrocracking catalyst activity damage, reaction temperature mismatch, etc., and achieve good passivation effect, The effects of suitable process conditions, reducing operational fluctuations and operational risks
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Embodiment 1
[0053] When the reaction temperature of the first bed of hydrocracking catalyst is 366°C, and the temperature difference T1 between the inlet and outlet of the first catalyst bed is 5°C, the nitrogen weight content of the catalyst in the first catalyst bed is 0.3%, Cool down to 310°C and feed refined oil with a nitrogen content of 450ppm. After the nitrogen content of the liquid phase effluent from the cracking section is constant at 50ppm, feed hydrogenated refined oil with a nitrogen content of ~10ppm, and then first raise the reaction temperature to 355°C , adjust the temperature, control the conversion rate to be constant at 35%, and stabilize for 48 hours; continue to adjust the reaction temperature, control the conversion rate to be constant at 50%, and stabilize for 48 hours; continue to adjust the reaction temperature, control the conversion rate to be constant at 55%, and stabilize for 48 hours Continue to adjust the reaction temperature, control the conversion rate to...
Embodiment 2
[0055] When the reaction temperature of the first bed of hydrocracking catalyst is 367°C, and the temperature difference T1 between the inlet and outlet of the first catalyst bed is 6°C, the nitrogen content of the catalyst in the first catalyst bed is 0.29%, and the temperature is lowered Feed refined oil with a nitrogen content of 310ppm to 317°C. After the nitrogen content of the liquid phase effluent from the cracking section is constant at 50ppm, feed hydrogenated refined oil with a nitrogen content of ~10ppm, and then first raise the reaction temperature to 355°C , adjust the temperature, control the conversion rate to be constant at 35%, and stabilize for 24 hours; continue to adjust the reaction temperature, control the conversion rate to be constant at 45%, and stabilize for 48 hours; continue to adjust the reaction temperature, control the conversion rate to be constant at 55%, and stabilize for 48 hours Continue to adjust the reaction temperature, control the convers...
Embodiment 3
[0057] When the reaction temperature of the first bed of hydrocracking catalyst is 367°C, and the temperature difference T1 between the inlet and outlet of the first catalyst bed is 4°C, the nitrogen content of the catalyst in the first catalyst bed is 0.35%, and the temperature is lowered Feed refined oil with a nitrogen content of 395ppm to 313°C. After the nitrogen content of the liquid phase effluent from the cracking section is constant at 80ppm, feed hydrotreated refined oil with a nitrogen content of ~10ppm, and then first increase the reaction temperature to 355°C. Adjust the temperature, control the conversion rate to be constant at 35%, and stabilize for 48 hours; continue to adjust the reaction temperature, control the conversion rate to be constant at 50%, and stabilize for 24 hours; continue to adjust the reaction temperature, control the conversion rate to be constant at 55%, and stabilize for 24 hours; Continue to adjust the reaction temperature, control the conv...
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