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Residue oil hydrogenation catalyst and preparation method thereof

A technology of residual oil hydrogenation and catalyst, which is applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, hydrocarbon oil cracking, etc. It can solve the problems of reduced mechanical strength, failure of active metals to reach a high accumulation layer, and channel collapse. , to achieve the effect of reducing polarity and free energy, weakening capillary pressure, and improving dispersion

Active Publication Date: 2019-06-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The bulk phase hydrogenation catalyst disclosed by CN102049265A adds ammonium bicarbonate during the co-precipitation process, and the bulk phase hydrogenation catalyst disclosed by CN102451703A adds carbon dioxide during the co-precipitation process to generate carbonate or bicarbonate. It releases a certain amount of gas during the roasting process. Under the impact of the gas, the pore volume and specific surface area of ​​the catalyst are increased, so that more metal active sites are exposed on the surface of the catalyst, but this method will cause some pores to collapse. , the pore distribution is dispersed, and the mechanical strength is reduced
This method is mainly to achieve uniform dispersion of active metals, but uniformly dispersed active metals cannot achieve a high number of stacked layers, which is quite different from the formation of highly active hydrogenation active centers

Method used

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  • Residue oil hydrogenation catalyst and preparation method thereof
  • Residue oil hydrogenation catalyst and preparation method thereof
  • Residue oil hydrogenation catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] (1) Weigh 100g of industrially produced residual oil hydrodemetallization catalyst carrier alumina, spray with 100ml of Span-80 ethanol solution with a concentration of 0.5g / 100ml, and then vacuum-dry at 60°C for 5 hours;

[0024] (2) Preparation of impregnation solution: add ammonium molybdate, nickel nitrate and phosphoric acid into water to dissolve, then add sodium polyacrylate to obtain an impregnation solution, in which the content of molybdenum oxide is 25.7 g / 100ml, and the content of nickel oxide is 5.8g / 100ml , the content of phosphorus is 2.1g / 100ml, and the content of sodium polyacrylate is 0.5 g / 100ml. The prepared impregnating solution was used to impregnate the above-mentioned dried catalyst carrier for 2 hours, then dried at 120° C. for 5 hours, and then calcined at 500° C. for 4 hours to obtain residual oil hydrogenation catalyst A.

Embodiment 2

[0026] Same as Example 1, except that when spraying with ethanol solution containing Span-80, the concentration of Span-80 used is the ethanol solution of 1.0g / 100ml, vacuum-dried at 60°C for 5 hours, and then use the ethanol solution of Example 1 The impregnation solution in 1 impregnates the dried support to obtain residue hydrogenation catalyst B.

Embodiment 3

[0028] Same as Example 1, except that the content of sodium polyacrylate in the prepared impregnation solution is 1.0g / 100ml, the impregnation time is 3 hours, then dried at 120°C for 5 hours, and roasted at 500°C for 4 hours to obtain Residue Hydrogenation Catalyst C.

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Abstract

The invention discloses a residue oil hydrogenation catalyst and a preparation method thereof, wherein the preparation method comprises: (1) carrying out spray impregnating on a residue oil hydrodemetallization catalyst carrier with an organic solvent containing a Span surfactant, and drying; and (2) impregnating the dried carrier with an active metal solution containing polyacrylate radicals, drying, and calcining to obtain the catalyst. According to the present invention, the residue oil hydrogenation catalyst prepared by the method has advantages of high metal utilization rate, high metal dispersion degree, high activity and the like.

Description

technical field [0001] The invention relates to a residual oil hydrogenation catalyst and its preparation, in particular to a residue oil hydrogenation catalyst with high metal dispersion and high activity and its preparation. Background technique [0002] With the increasingly heavy and inferior crude oil at home and abroad, residual oil hydrotreating technology has been increasingly widely used. At present, the industrially used residual oil hydrotreating catalysts usually use alumina or alumina containing a small amount of additives as the carrier, and the metal elements of Group VIII and Group VIB as active components. In the preparation process of residual oil hydrogenation catalyst, it is generally prepared by impregnating the aqueous solution of metal compound one or more times through the carrier, and then drying and roasting. This catalyst preparation method is described in EP0469675, etc., for example. [0003] During the catalyst impregnation process, the pores o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/19B01J35/10B01J37/02B01J37/08C10G47/12
Inventor 刘文洁张庆军刘涛隋宝宽袁胜华
Owner CHINA PETROLEUM & CHEM CORP
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