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Startup passivation method of hydrocracking catalyst

A hydrocracking and catalyst technology, applied in hydroprocessing process, petroleum industry, hydrocarbon oil treatment, etc., to achieve the effect of energy saving, rational utilization of resources, avoidance of emissions or follow-up treatment

Active Publication Date: 2013-04-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the problems existing in the existing start-up technology, the present invention provides a start-up method for passivating the vulcanized hydrocracking agent by using a light oil product containing relatively high nitrogen content as a passivating agent. The ammonia gas generated by the hydrogen denitrification reaction is adsorbed on the cracking agent, the passivation process is completed and the start-up is successful, which can completely avoid the consumption of the passivation agent during the start-up process, which not only saves energy, but also reduces the impact of the passivation agent on the environment. Pollution and harm to the human body

Method used

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  • Startup passivation method of hydrocracking catalyst

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Embodiment approach

[0024] Such asfigure 1 As shown, an embodiment of the hydrocracking catalyst start-up passivation method of the present invention is as follows:

[0025] After the light oil 1 with relatively high nitrogen content is mixed with hydrogen 2, it enters the hydrofining reactor 3 with an inlet temperature of 150-205°C, and the product 6 obtained after the reaction effluent 4 passes through the cooling heat exchange system 5 enters the separation system 7. The gas phase 9 obtained at the top goes to the hydrogen compressor, and the liquid phase 8 obtained by the separation system 7 enters the fractionation system 10, and after fractionation, the product exits the device; When the temperature rises higher, it generally exceeds 100°C. At this time, the product 4 obtained at this time passes through the heat exchange cooling system 5 and then lowers the temperature to about 200°C to obtain the product 11, which is mixed with the circulating hydrogen 12 and then enters the hydrocracking ...

Embodiment 1

[0028] use figure 1 process shown. After the sulfidation of the catalyst is completed, the inlet temperatures of the refining reactor and the cracking reactor are respectively lowered to 200°C and 180°C.

[0029] Introduce coking naphtha into the refining reactor, increase the temperature of the refining reactor at a rate of 15°C / h, and the refined effluent directly enters the separation system; when the temperature rise of the refining reactor reaches 130°C and is stable, the refined effluent is replaced The heat enters the cracking reactor, and the inlet temperature of the cracking reactor is maintained not higher than 205°C, waiting for ammonia to penetrate.

[0030] When the ammonia concentration in the water of the separation system reaches 0.5wt%, the inlet temperature of the cracking reactor is increased at a rate of 6°C / h through heat exchange, and the ammonia concentration in the water of the separation system is kept above 0.5wt% during the temperature rise; when th...

Embodiment 2

[0034] Main process is with embodiment 1. After the sulfidation is completed, the temperatures of the refining reactor and the cracking reactor are lowered to 180°C and 150°C respectively.

[0035] When the temperature rise of the refining reactor reaches 150° C. and stabilizes, the refining effluent is passed through the cracking reactor.

[0036] Other operations can be carried out according to Example 1.

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Abstract

The invention discloses a startup passivation method of a hydrocracking catalyst. The method includes: after the end of vulcanization, lowering the inlet temperature of a refining reactor and a cracking reactor to 150-205DEG C; introducing high-nitrogen naphtha into the refining reactor, and leaving the refined effluent to enter a separation system; raising the inlet temperature of the refining reactor, and when the refining section has high and stable temperature rise, making the refined effluent enter the cracking reactor after heat exchange, and maintaining a constant cracking reactor inlet temperature; after ammonia penetrates the cracking reactor, adjusting the refining reactor inlet temperature and heat exchange operations, and slowly raising the inlet temperature of the cracking reactor till 300-320DEG C, thus finishing passivation. The method disclosed in the invention introduces the high-nitrogen naphtha into the refining section in the catalyst passivation stage, and adopts the ammonia gas generated by hydrogenation of the high-nitrogen naphtha as a passivant to passivate a cracking agent, thus reaching the purpose of using no passivant. The method provided in the invention is applicable to the principle-based startup passivation process of various hydrocracking catalysts.

Description

technical field [0001] The invention relates to a start-up passivation method of a hydrocracking catalyst, which mainly uses light oil products containing relatively high nitrogen content as a passivation agent to passivate the hydrocracking agent, so as to achieve the purpose of not using a passivation agent , The principle of starting passivation process applicable to various hydrocracking catalysts. Background technique [0002] The hydrocracking process is under the action of hydrogen, high temperature, high pressure and catalysts to hydrodesulfurize, hydrodenitrogenate, polycyclic aromatic hydrocarbons, hydrosaturation and ring-opening cracking of heavy distillate oils (VGO, CGO, DAO). The process of conversion into target products such as light oil and middle distillates. The hydrocracking catalysts currently produced in domestic industry are basically oxidative. New catalysts or regenerated catalysts produced in industry contain active metal components (Mo, Ni, Co, ...

Claims

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Application Information

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IPC IPC(8): C10G67/00
Inventor 王仲义彭冲潘德满石友良吴子明孙士可
Owner CHINA PETROLEUM & CHEM CORP
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