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Passivation method of sulfuration type hydrocracking catalyst

A hydrocracking and catalyst technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, catalyst activation/preparation, heterogeneous catalyst chemical elements, etc., can solve the problem of unstable and unsafe molecular sieve passivation process Health and environmental protection, can not guarantee the passivation effect and other issues, to achieve good temporary passivation effect, efficient and stable passivation effect, avoid the effect of passivation instability

Pending Publication Date: 2021-10-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, anhydrous liquid ammonia is an irritating and toxic liquid, which is flammable and explosive. It is dangerous to use anhydrous liquid ammonia in industry. If it leaks, it will cause great harm to the environment and people. The concept of safety, health and environmental protection
[0005] CN107446616A discloses a method of loading low-molecular nitrogen compounds on conventional hydrocracking catalysts or introducing low-molecular nitrogen compounds during the catalyst kneading molding process to alleviate the risk of overheating during the start-up process of the hydrocracking unit, but the catalyst is in Vulcanization treatment is also required during the start-up process, which will cause some nitrides to react with sulfides during the vulcanization process or desorb in advance as the vulcanization temperature increases, and there is no subsequent ammonia injection process, resulting in molecular sieve passivation process Unstable, the passivation effect cannot be guaranteed, and there is still a certain risk of overheating

Method used

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  • Passivation method of sulfuration type hydrocracking catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Take 200g of oxidative hydrocracking catalyst, carry out sulfuration treatment outside the device, and convert it into sulfurized hydrocracking catalyst for future use.

[0028] Take 100g of sulfide-type hydrocracking catalyst, add 13.2g of tri-n-butylamine and 1.5g of dimethyl disulfide into diesel oil, stir evenly at 45°C to obtain a solution containing nitrogen and sulfur, and follow the method of pore saturation impregnation , introducing nitrogen and sulfur solution into sulfurized hydrocracking catalyst to introduce nitrogen content of 1.0% by weight and sulfur content of 1.0% by weight to obtain a catalyst loaded with nitrogen and sulfur; then at 40°C, under normal pressure, flowing Passivation treatment was carried out for 4 hours under air atmosphere to prepare passivated catalyst C1.

[0029] Put the passivated catalyst C1 into the reactor for reaction, when the temperature rises to 100°C, feed hydrogen and n-heptane raw materials, continue to raise the temper...

Embodiment 2

[0031] Take 100g of the same sulfurized hydrocracking catalyst as in Example 1, add 26.4g of tri-n-butylamine and 1.2g of carbon disulfide into the lubricating base oil, and stir evenly at 30°C to obtain a nitrogen- and sulfur-containing solution. Saturated impregnation method, introducing nitrogen and sulfur solution into sulfurized hydrocracking catalyst to introduce nitrogen content of 2.0% by weight and sulfur content of 1.0% by weight to obtain catalyst loaded with nitrogen and sulfur; then at 40°C, 0.1MPa Passivation treatment was carried out for 4 hours under pressure and in a non-flowing nitrogen atmosphere to prepare a passivated catalyst C2. The deactivated catalyst C2 was loaded into the reactor for reaction under the same reaction conditions as in Example 1, and its hydrocracking activity (expressed in the form of conversion rate) is shown in Table 1.

Embodiment 3

[0033] Get 100g of the same sulfurized hydrocracking catalyst as in Example 1, add 13.2g of dodecylamine and 0.75g of dimethyl disulfide into diesel oil, stir evenly at 60°C, and obtain a nitrogen- and sulfur-containing solution. Pore ​​saturation impregnation, introducing nitrogen and sulfur solution into sulfurized hydrocracking catalyst to introduce nitrogen content of 1.0% by weight and sulfur content of 0.5% by weight to obtain a catalyst loaded with nitrogen and sulfur; then at 60°C, 0.1 Passivation treatment was carried out for 2 hours under MPa pressure and in a stagnant air atmosphere to prepare a passivated catalyst C3. The deactivated catalyst C3 was loaded into the reactor for reaction under the same reaction conditions as in Example 1, and its hydrocracking activity (expressed in the form of conversion rate) is shown in Table 1.

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Abstract

The present invention relates to a passivation method of a vulcanization type hydrocracking catalyst , which comprises the steps of: loading a sulfur-containing compound and a nitrogen-containing compound onto a vulcanization type hydrocracking catalyst, and carrying out passivation treatment. Due to the loading, the nitrogen content of the sulfuration type hydrocracking catalyst before passivation treatment is 0.1-5wt% in terms of element, and the sulfur content of the sulfuration type hydrocracking catalyst before passivation treatment is 0.1-5wt% in terms of element. The passivating treatment conditions are as follows: the temperature is 10-120 DEG C, the pressure is 0.01-0.5 MPa, and the time is 0.5-10 hours. The method provided by the invention is good in passivation effect, the catalyst prepared by the method provided by the invention is free of desulfurization reaction during startup, the reaction activity is high, and the startup time of a hydrogenation device is shortened.

Description

technical field [0001] The invention relates to an external passivation method of sulfurized hydrocracking catalyst and a hydrocracking catalyst prepared by the method. Background technique [0002] Hydrocracking technology is an effective means of converting heavy distillate oil into light clean products, therefore, the number of hydroprocessing units in major refineries is also increasing. Hydrocracking technology uses dual-functional catalysts, including cracking function and hydrogenation function. The cracking function is usually provided by molecular sieves with acidic sites, and the hydrogenation function mainly comes from active metals, including Co and / or Ni of group VIII, VIB Mo and / or W of the group. The hydrogenation catalyst has high hydrogenation performance only when the metal is converted into a sulfurized state. Therefore, in order to optimize the hydrogenation performance of the catalyst, the catalyst needs to be sulfurized before use. At present, the sul...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J37/02B01J29/16C10G45/12
CPCB01J37/0203B01J29/166B01J23/002C10G45/12C10G2300/202C10G2300/1037B01J2523/00B01J2523/31B01J2523/69B01J2523/847
Inventor 翟维明刘锋晋超杨平褚阳杨清河
Owner CHINA PETROLEUM & CHEM CORP
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