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Residual oil hydrotreating method

A technology of residual oil hydrogenation and treatment method, which is applied in refining to remove heteroatoms, etc., can solve the problems of waste of post catalyst activity resources, etc., and achieve the effects of good operating flexibility, increased ratio, and reduced circulation resistance

Active Publication Date: 2014-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] However, in the above-mentioned related patent technologies, no matter whether a special-shaped catalyst is used to increase the bed porosity, or an upflow reactor is used, the reactant flow still flows along the axial direction of the reactor, and the ratio of the flow area to the flow path is relatively small and is a fixed value. , the solid deposits first coalesce in the pre-catalyst bed, and gradually extend to the post-catalyst bed, which cannot fundamentally solve the problems of simultaneous catalyst deactivation and high pressure drop in the catalyst bed, and the waste of active resources of the post-catalyst problem always exists

Method used

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  • Residual oil hydrotreating method

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Effect test

Embodiment 1

[0038] The same catalyst type and its loading method were used to compare the operating elasticity of the radial-flow fixed bed of the present invention and the existing fixed bed residue hydrogenation technology.

[0039] In this example, the residue hydrogenation catalyst developed and produced by Fushun Petrochemical Research Institute (FIRPP) was used. The protective agent was FZC-13, the hydrodemetallization catalyst was FZC-21, and the hydrodesulfurization catalyst was FZC-30. , the hydrodenitrogenation catalyst is FZC-41, and in the catalyst bed, the loading ratio of various functional catalysts is FZC-13:FZC-21:FZC-30:FZC-41=13:32:20:35. The raw material oil is a Middle Eastern atmospheric residue, and its impurity content is as follows: S=2.78m%, N=0.29m%, CCR=12.1m%, Ni+V=110μg / g. The reaction conditions are: reaction pressure 15.7MPa, reaction temperature 370°C, hydrogen-to-oil volume ratio 700, and the oil feed rate is 0.2h at the existing fixed bed space velocity ...

Embodiment 2

[0048] Using the same catalyst species and loading method as in Example 1, the stability comparison between the radial-flow fixed bed technology of the present invention and the existing fixed bed residual oil hydrogenation technology was carried out.

[0049] In this example, a batch of residual oil hydrogenation catalysts prepared by FIRPP laboratory is used. The protective agent is FZC-14, the hydrodemetallization catalyst is FZC-28, the hydrodesulfurization catalyst is FZC-34, and the hydrodenitrogenation catalyst is FZC-34. The catalyst is FZC-42, and the gradation of each catalyst in the reactor is FZC-14:FZC-28:FZC-34:FZC-42=13:32:23:32. The raw material oil is another Middle Eastern atmospheric residue, and its impurity content is as follows: S=2.67m%, N=0.31m%, CCR=13.57m%, Ni+V=126μg / g. The reaction conditions are: reaction pressure 15.7MPa, reaction temperature 375°C, hydrogen-to-oil volume ratio 700, and the oil feed rate is 0.2h at the space velocity of the existi...

Embodiment 3

[0058] Using the same catalyst type and its loading method, the relationship between the running time and temperature of the radial-flow fixed bed of the present invention and the existing fixed bed residual oil hydrogenation technology is carried out.

[0059] Adopt the same raw material and catalyzer among the embodiment 1 among the embodiment 3. The reaction pressure is 15.7MPa, the volume ratio of hydrogen to oil is 700, and the space velocity is 0.2h -1 , The reaction temperature is 365°C.

[0060] Table 5 Results of residual oil hydrogenation method of the present invention

[0061] running time, h 1000 2000 4000 Reaction temperature, °C 365 365 365 Desulfurization rate, % 80.20 80.23 80.31 Nitrogen removal rate, % 46.23 46.27 46.38 Carbon residue removal rate, % 53.62 53.66 53.71 Stripping (nickel + vanadium) rate, % 81.35 81.40 81.51 Differential pressure, kPa 0 0 0

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Abstract

The invention discloses a residual oil hydrotreating method, the method uses a fixed bed radial reactor for residual oil hydrogenation reaction, catalyst bed layers of the fixed bed radial reactor are respectively loaded, from the inside to the outside, with a protective agent, a hydrodemetallization catalyst, a hydrodesulfurization catalyst and a hydrodenitrogenation / carbon residue removal catalyst, raw oil mixed with dissolved hydrogen enters from the reactor bottom via a feed tube for hydrotreating reaction, hydrogenated generation oil is collected by a generation oil collection zone, and then discharged out of the reactor. The method avoids the defects that in the prior art, when the hydrodemetallization activity of a front catalyst of a fixed bed residual oil hydrogenation unit is lost, hydrodemetallization reaction is undertaken completely by a rear catalyst, and the rear catalyst deactivation is accelerated, overall improves the active resource utilization rate of catalysts, and can effectively reduce the varieties and specifications of the catalysts without too much increase of the protective agent, the raw oil can be in stable and long-term operation at the optimum reaction temperature, and temperature increasing operation is not needed for compensation of the catalyst activity.

Description

technical field [0001] The invention relates to the technical field of residue oil hydrogenation, in particular to a method for hydrogenating residue oil using a fixed-bed radial reactor. Background technique [0002] Hydrogenation of residual oil is one of the main technical approaches to lighten heavy oil. At present, hydrogenation reaction technologies such as fixed bed, moving bed, ebullating bed, and suspension bed have been developed for residual oil hydrogenation. Among them, fixed-bed hydrogenation technology has developed rapidly with the main technical advantage of simple and stable reaction process operation, and has become the most mature mainstream technology for residual oil hydrogenation. More and more refineries choose fixed-bed residual oil hydrogenation and residual oil catalytic cracking The combined process achieves the purpose of producing high-quality gasoline, kerosene, and diesel in a large amount, and the economic and social benefits are remarkable....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/02
Inventor 彭派耿新国刘铁斌李洪广曾榕辉蒋立敬袁胜华郭蓉
Owner CHINA PETROLEUM & CHEM CORP
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