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Boiling bed hydrogenation treatment catalyst and its preparing process

A hydrogenation treatment and catalyst technology, which is applied in the fields of refining hydrocarbon oil, petroleum industry, refining to remove heteroatoms, etc., can solve the problems of difficulty in preparing spherical catalysts, low production efficiency, and difficulty in cutting rods, etc., and achieve various Excellent performance indicators, high production efficiency, and good physical and chemical properties

Active Publication Date: 2008-08-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In fact, this method is suitable for preparing spherical particles with a diameter of more than 2 mm, but it is difficult to prepare spherical particles smaller than 1 mm, because it is difficult to prepare rods on grooves smaller than 1 mm, and it is difficult to cut rods. The production efficiency of this method is also low. lower

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Weigh 1000g of pseudo-boehmite dry rubber powder and 34.5g of carbon black, add them into a kneader, and mix well. It was then mixed with 8 g of nitric acid (67w%), 39.82g of phosphoric acid (85w%) and 900g of water. After kneading into a plastic body, take it out and send it to the silo of the granulation device. The drum in the silo is rotated forward and reverse through mechanical transmission, and the material is extruded from the 40-mesh screen to make small particles with uniform particle size, and then Put the granules into the spherical granulator, feed air, process at 50 rpm for 5 minutes, and then at 600 rpm for 15 minutes, so that the granules are transformed into spherical objects, and the granules have no obvious growth phenomenon, spherical The object diameter is about 0.2mm. The spheres were dried at 120°C for 4 hours and calcined at 800°C for 2 hours to obtain catalyst support S1. The carrier yield (the amount of particles between 40-100 meshes to the ...

Embodiment 2

[0033] In embodiment 1, 39.82g phosphoric acid is changed into the boric acid of 47.56, changes 60 mesh sieves, extrudes small particle and carries out balling process after placing under stirring condition for 30 minutes, obtains microsphere diameter and is about 0.16mm, other and embodiment 1 Similarly, the catalyst carrier S2 was obtained.

[0034] The active metal was loaded according to the method described in Example 1 to obtain catalyst C2.

Embodiment 3

[0036] In embodiment 1, the pseudoboehmite dry rubber powder was changed to aluminum dry rubber powder with a Si weight content of 4%, and the extruded small particles were processed at 250 rpm for 3 minutes, and then at 500 rpm for 20 minutes. The particles were converted into spherical objects, and the others were the same as in Example 1 to obtain carrier S3.

[0037] It was impregnated with Mo and Ni solutions by equal volume method, then dried at 120°C for 4 hours, and calcined at 500°C for 2 hours to obtain the final catalyst C3.

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Abstract

The invention relates to a boiling bed hydrogenation catalyst and a preparation method. The boiling bed hydrogenation catalyst of the invention is spherical shape which diameter is 0.1mm to 0.8mm, and has appropriate amount of additives and hydrogenation of metal components, and has reasonable hole distribution. The catalyst preparation method of the invention is spherical carrier impregnation, the process of spherical carrier preparation is following: making catalyst carrier raw material which is in appropriate temperature into appropriate size grain, then spheroidizing the grain, heating the conglobation and making them into spherical catalyst carrier. The process for making the catalyst carrier raw material into the appropriate size grain is that wet stock passes screen stencil by mechanical action and generates grain. Between the processes of the making grain and nodularization, granular material primely is placed for a period of time or operates in low-speed in nodularization device for a period of time. The catalyst of the invention appropriately conducts the boiling bed hydrogenation for heavy oil, residual oil.

Description

technical field [0001] The invention relates to a fluidized bed hydrogenation treatment catalyst and a preparation method thereof, in particular to a fluidized bed hydrogenation treatment catalyst used for heavy oil, especially residual oil with relatively high metal content, and a preparation method thereof. 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. Hydrogenation and upgrading of residual oil mainly include fixed bed, moving bed and ebullating bed hydrogenation processes. Fixed bed is widely used because of its mature technology and simple operation. However, the residual oil fixed bed hydrogenation process has strict restrictions on the content of metals and residual ca...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/20C10G45/04
Inventor 孙素华朱慧红刘杰杨光张成
Owner CHINA PETROLEUM & CHEM CORP
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