Heavy raw material boiling bed hydrogenation treatment method

A hydroprocessing and ebullating bed technology, which is applied in the treatment of hydrocarbon oil, petroleum industry, refining to remove heteroatoms, etc., can solve the problems of increased reactor scale, inability to optimize hydrogenation performance, unstable operation, etc., and achieve High hydrodesulfurization activity and metal removal activity, suitable asphaltene conversion performance, and the effect of improving comprehensive reaction performance

Active Publication Date: 2012-05-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
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  • Application Information

AI Technical Summary

Problems solved by technology

Although the ebullating bed reactor and method realize the use of multiple ebullating bed catalysts in one reactor, a large number of internal components are used in the reactor, which on the one hand causes complex structure and high equipment cost, and on the other hand causes the volume utilization of the reactor to be low. Low, increased reactor scale, unstable operation, etc.
Although the pore structure of ebullating bed catalysts can be adjusted using existing technologies, it is generally not easy to adjust the distribution of large pores and small pores for the same catalyst.
In addition, the hydrogenation active metal components in the large and small pores cannot be optimized and adjusted, so it is not suitable for flexible optimization of the hydrogenation performance required for different pore sizes.

Method used

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  • Heavy raw material boiling bed hydrogenation treatment method
  • Heavy raw material boiling bed hydrogenation treatment method

Examples

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preparation example Construction

[0016] The preparation process of the ebullated bed hydrotreating catalyst is to firstly prepare the microspherical catalyst carrier, and then use the impregnation method to support the required hydrogenation active metal components. The preparation process of the catalyst carrier is as follows: the raw materials of the catalyst carrier with suitable humidity are made into particles of suitable size, and then the particles are spheroidized, and the spheres are dried and calcined to form a spherical catalyst carrier.

[0017] The drying and calcination of the catalyst carrier can adopt conditions well known to those skilled in the art, such as natural drying or drying at 80-150°C, and calcination at 600-1000°C for 1-6 hours. The impregnation method to support the active hydrogenation metal component can be carried out by methods well known to those skilled in the art, such as making a solution of the required active metal salt, impregnating the catalyst carrier with the solution...

Embodiment 1

[0021] Catalyst preparation

[0022] 1. Preparation of Catalyst A

[0023] Prepare a spherical catalyst carrier with an average pore diameter of 22nm and a spherical particle diameter of 0.4mm. Other catalyst preparation processes refer to US4328127 and CN200710010377.5.

[0024] Prepare the Mo-Ni solution according to the conventional method, and the MoO in the solution 3 The NiO content is 4.01%, and the NiO content is 1.03%. The above-mentioned carrier was impregnated with this solution by an equal-volume impregnation method to obtain the final catalyst A, whose properties are shown in Table 1.

[0025] 2. Preparation of Catalyst B

[0026] A spherical catalyst carrier with an average pore diameter of 11nm was prepared, and the spherical catalyst particle size was 0.4mm. Other catalyst preparation processes were carried out according to the methods of US7074740 and CN200710010377.5.

[0027] Prepare the Mo-Co-P solution according to the conventional method, and the MoO ...

Embodiment 2

[0029] Catalysts A and B in Example 1 were selected and mixed in a ratio of 1:0.5 by volume and loaded into a 1L autoclave, and a vacuum residue hydrotreating test was carried out in the presence of hydrogen. The properties of the vacuum residue selected for the test are: distillation range 520°C + , the sulfur content is 2.8wt%, the metal (Ni+V+Fe) content is 357μg / g, and the asphaltene content is 6.8%. The test conditions are: reaction temperature 408°C, reaction pressure 13MPa, reaction time 0.5h, oil agent volume ratio 15, evaluation results are shown in Table 2.

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Abstract

The invention relates to a heavy raw material boiling bed hydrogenation treatment method. A boiling bed hydrogenation treatment reactor is used, the heavy oil raw material oil and hydrogen gas enter a reactor from the bottom, the reaction is carried out under the heavy raw material oil hydrogenation treatment condition, materials after the reaction are discharged out from the reactor from the top, a mixed catalyst of at least two catalysts is used in the boiling bed hydrogenation treatment reactor, and the mixed volume is 1:(0.1-10). One catalyst has the properties that the specific surface is 80 to 200 mm<2> / g, the several-hole diameter can be 15 to 30nm, and holes with the hole diameter being 30 to 300nm account for 35 percent to 60 percent of the total hole volume. The other catalyst has the properties that the specific surface is 180 to 300 mm<2> / g, and holes with the hole diameters being 5 to 20nm at least account for 70 percent of the total hole volume. The method has the advantages that the operation performance of the boiling bed slag oil hydrogenation treatment process can be effectively improved, and the hydrogenation activity level and the operation flexibility are improved.

Description

technical field [0001] The invention relates to a method for hydrotreating heavy raw oil in a fluidized bed, in particular to a hydroprocessing process in a fluidized bed used for low-quality residual oil with high heavy metal content. Background technique [0002] With the gradual reduction of petroleum resources, the increasing demand for light oil and the increasingly stringent environmental regulations, the refining industry attaches great importance to the rational use of petroleum resources, which greatly promotes the development of residual oil hydroprocessing technology. The hydro-upgrading of heavy raw oil mainly includes fixed-bed, moving-bed, and ebullating-bed hydrogenation processes. In the fluidized bed hydrogenation process, the catalyst can be added and discharged online, which is conducive to maintaining high catalyst activity and long-term operation. It has strong adaptability to raw materials, flexible processing schemes, and can process inferior raw mater...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/08C10G49/04
Inventor 孙素华朱慧红刘杰杨光
Owner CHINA PETROLEUM & CHEM CORP
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