Start-up presulfidation method of hydrogenation catalyst

A hydrogenation catalyst and catalyst technology, which is applied in the petroleum industry, hydrocarbon oil cracking, etc., can solve the problems of difficulty in ensuring the oxidation state, cracking activity and activity stability of elemental metal catalysts, low decomposition temperature, and high relative density, and achieve saving manpower, increase the concentration of hydrogen sulfide, avoid the effect of emission

Active Publication Date: 2015-09-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Carbon disulfide (CS 2 ) has high sulfur content, low decomposition temperature, and relatively cheap price; because of its low boiling point, high relative density (1.26), and almost insoluble in water, it is generally stored in a storage tank with water and sealed, which is relatively safe to use, but toxic Larger; although the sulfur content of DMDS is low, the decomposition temperature is high, and the toxicity is slightly small, it still has certain harmfulness to the human body and should not be excessively contacted with it.
[0006] CN101003749A introduces a hydrocracking start-up method that does not require the use of vulcanizing agents in the whole process. Although the operation is simple and the process is easy, it is difficult to ensure the oxidation state and the cracking activity and activity stability of the elemental metal catalyst

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  • Start-up presulfidation method of hydrogenation catalyst

Examples

Experimental program
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Embodiment approach

[0034] Such as figure 1 As shown, an embodiment of the hydrogenation catalyst start-up method of the present invention is as follows:

[0035] Raise the inlet temperature of the refining reactor 13 to 170-190°C. Sulfur-containing exhaust gas 1 passes through light hydrocarbon absorption tower 2 for light hydrocarbon recovery, absorbing liquid heavy naphtha 4 is injected into the top of the tower, mixed naphtha 5 is discharged from the bottom of the tower to analyze and stabilize the system, and the absorbed gas is injected into the In high pressure separator 6. Then the obtained high-fraction gas is adjusted by hydrogen sulfide through the circulating hydrogen desulfurization tower 7, the top of the tower is injected with lean amine liquid 8, and the bottom of the tower is discharged with rich amine liquid 9, and the concentration of hydrogen sulfide is controlled at 0.5-1.5v% by washing, and then mixed with new hydrogen 11 is mixed to obtain mixed hydrogen 12, which enters ...

Embodiment 1

[0037] The properties of the catalysts used in Examples 1, 2 and Comparative Examples 1, 2 are listed in Table 1. The catalyst is a commercial catalyst developed and produced by Fushun Petrochemical Research Institute, wherein Example 1 and Example 2 are the start-up method of the present invention, Comparative Example 1 is a conventional dry start-up process, and Comparative Example 2 is the use of acidic acid rich in inert gas in a refinery. Air-drying start-up process.

[0038] Table 1 Main physicochemical properties of catalysts

[0039] project FF-36 FC-14 Chemical composition, wt% Mo-Ni W-Ni NiO 4.0 5.5 MoO 3 25.0 — WO 3 — 22.0 physical properties Appearance shape Clover Strips Cylindrical bar Crushing strength, N / cm ≥180 >185

[0040] Example 1

[0041] After the hydrogen airtightness of the hydrocracking unit is qualified, adjust the inlet pressure of the reaction system to 14.0MPa, start to...

Embodiment 2

[0043] After the hydrogen airtightness of the hydrocracking unit is qualified, adjust the inlet pressure of the reaction system to 12.0MPa, start to raise the temperature at 20°C / h, and when it reaches 170°C, pass the mixed acid gas into the light hydrocarbon absorption system for absorption, and then start the sulfidation The hydrogen compressor injects the absorbed gas into the high fraction, and the high fraction gas first passes through the circulating hydrogen desulfurization tower, and then enters the reaction system through the compressor. Adjust the operation of the circulating hydrogen desulfurization tower to control the H in the circulating hydrogen 2 The S concentration is 0.8v%, and when the hydrogen sulfide concentration at the outlet of the hydrocracking reactor reaches 0.11v%, it is considered that the hydrogen sulfide has penetrated the catalyst bed. Adjust the catalyst bed temperature to 230°C and keep the temperature constant for 8 hours. This process adjust...

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Abstract

The invention discloses a startup presulfurization method of a hydrogenation catalyst. The method consists of: collecting the sulfur-containing effluent gas of a refinery plant, first conducting light hydrocarbon absorption to remove the light hydrocarbon with a high content of C1-C4, and enhancing the hydrogen purity and hydrogen sulfide concentration; then mixing the effluent gas with a circulating gas in a high pressure separator, and passing the gas generated in the high pressure separator through a circulating hydrogen desulfurization tower; and adjusting the operations on the desulfurization tower to control the concentration of hydrogen sulfide in circulating hydrogen, thus finishing sulfurization of the hydrogenation catalyst. The method provided in the invention can, on the one hand, cancel the consumption of a sulfurization agent, and on the other hand can perform optimization treatment on the sulfur-containing effluent gas, so that a more convenient and economical approach can be found for governance of sulfur-containing exhaust gases from refinery plants while startup sulfurization of hydrogenation equipment is completed.

Description

technical field [0001] The invention relates to a start-up vulcanization method of a hydrocracking catalyst, which mainly uses the low fraction gas and tail gas of an industrial hydrogenation device as a source of hydrogen sulfide to carry out start-up vulcanization of the catalyst, so as to achieve the purpose of not using a vulcanizing agent, and is suitable for Principled start-up process for hydrocracking catalysts in various oxidation states. Background technique [0002] At present, due to the increasingly heavy crude oil in the world and the strict requirements of environmental protection regulations, the hydrogenation type devices have grown rapidly at a rapid rate. The amount of waste gas is also increasing day by day. For this kind of gas, the treatment methods have always been relatively simple, the utilization rate is not high, and the waste is serious, which has caused a serious burden on the energy saving, emission reduction, and efficiency enhancement of enter...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G47/00
Inventor 王仲义彭冲潘德满石友良黄新露吴子明孙士可
Owner CHINA PETROLEUM & CHEM CORP
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