Rapid start-up method of hydrocracking catalyst
A hydrocracking and catalyst technology, which is used in hydrocarbon oil cracking, petroleum industry, etc., can solve the problems of difficult control and control, influence of catalyst activity, waste of floor space, etc., to reduce operating fluctuations and operating risks, and accelerate initial activity. The effect of stabilizing the process and stabilizing the catalyst activity
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[0034] Example 1
[0035] According to the start-up process of the conventional hydrocracking unit, the reactor inlet temperature was controlled at 160°C, low nitrogen oil was introduced into the reaction system, the reactor inlet temperature was raised to 180°C, and the sulfiding agent was injected into the reaction system. After the hydrogen sulfide concentration in the circulating hydrogen reaches 0.1v%, the inlet temperature of the reactor is increased to 220°C, and the constant temperature vulcanization is at least 8 hours. Then the temperature was raised to 270°C to introduce the feed oil and changed to a one-pass process to continue vulcanization, and the temperature was increased to 320°C at a temperature rise rate of 8°C / hour, and the vulcanization was completed after 4 hours of constant temperature. Then, the reaction temperature was first increased to 355°C, and the temperature was adjusted to control the conversion rate to be constant at 35% and stable for 2 days. Th...
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[0036] Example 2
[0037] According to the start-up process of the conventional hydrocracking unit, the reactor inlet temperature was controlled at 160°C, low nitrogen oil was introduced into the reaction system, the reactor inlet temperature was raised to 180°C, and the sulfiding agent was injected into the reaction system. After the hydrogen sulfide concentration in the circulating hydrogen reaches 0.1v%, the inlet temperature of the reactor is increased to 240°C, and constant temperature vulcanization is performed for at least 8 hours. Then the temperature was increased to 280°C to introduce the feedstock oil and changed to a one-pass process to continue vulcanization. The temperature was increased to 330°C at a temperature rise rate of 8°C / hour, and the vulcanization was completed after 4 hours of constant temperature. Then, the reaction temperature was first increased to 365°C, and the temperature was adjusted to control the conversion rate to be constant at 35% and stabiliz...
Example Embodiment
[0038] Example 3
[0039] According to the start-up process of the conventional hydrocracking unit, the reactor inlet temperature was controlled at 160°C, low nitrogen oil was introduced into the reaction system, the reactor inlet temperature was raised to 180°C, and the sulfiding agent was injected into the reaction system. After the hydrogen sulfide concentration in the circulating hydrogen reaches 0.1v%, the inlet temperature of the reactor is increased to 220°C, and the constant temperature vulcanization is at least 8 hours. Then the temperature was raised to 270°C to introduce the feedstock oil and changed to a one-pass process to continue the vulcanization. The temperature was increased to 320°C at a temperature rising rate of 8°C / hour, and the vulcanization was completed after 8 hours of constant temperature. Then, the reaction temperature was first increased to 360°C, and the temperature was adjusted to control the conversion rate to be constant at 40% and stabilize for 2...
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