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Preparation method of phosphoric hydrogenation catalyst for realizing deep desulfurization and denitrification

A hydrogenation catalyst and catalyst technology, applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem of weakening the interaction of active components, few new preparation methods, and reducing active components Dispersion and other issues, achieve weak interaction, high dispersion, and overcome the effect of active component agglomeration

Active Publication Date: 2011-01-12
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the current publicly reported technologies, most of the impregnation methods are used to prepare phosphorus-containing hydrofining catalysts. Although the interaction between the active component and the carrier can be weakened, the impact of the impregnation method itself also significantly reduces the interaction between the active component and the support. Dispersion
By introducing more metal active components and using a new type of non-alumina carrier, although the performance of the catalyst can be improved, it will bring a series of negative problems, such as cost, stability, etc.
On the other hand, from the prior art reports cited above, it can be seen that most of the researchers' improvements to hydrofining catalysts focus on the improvement of active components and supports, and there is a lot of research on new preparation methods for introducing phosphorus into catalysts. few

Method used

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  • Preparation method of phosphoric hydrogenation catalyst for realizing deep desulfurization and denitrification
  • Preparation method of phosphoric hydrogenation catalyst for realizing deep desulfurization and denitrification

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Weigh shaped γ-Al 2 o 3Put 5g of carrier into a 100ml autoclave, add 1.9ml of 0.3mol / l ammonium metatungstate solution, then add 6.8ml of 2.0mol / l nitric acid, stir evenly, then add 0.8mol / l citric acid solution 15.5ml and 4ml of ammonium phosphate solutions with a concentration of 0.52mol / l, closed the reaction vessel, heated up to 190°C, and stirred for 11 hours; cooled to room temperature, opened the reaction vessel, filtered the suspension, washed with water, and obtained solid product at 110 ℃ drying for 2 hours and calcination at 550℃ for 4 hours to obtain phosphorus-containing W / Al 2 o 3 catalyst.

[0026] To the phosphorus-containing W / Al 2 o 3 Add 4ml of nickel salt solution containing 0.7g of nickel nitrate hexahydrate, soak at room temperature for 12 hours, then dry at 110°C for 2 hours, and bake at 550°C for 4 hours to obtain phosphorus-containing NiW / Al 2 o 3 Hydrofining catalyst P1, the mass content and composition of the catalyst are listed in Tabl...

Embodiment 2

[0028] Weigh shaped γ-Al 2 o 3 Put 5g of carrier into a 100ml autoclave, add 23.0ml of 0.3mol / l sodium tungstate solution, then add 5.7ml of 2.4mol / l hydrochloric acid, stir well, add 17.2ml of 0.8mol / l oxalic acid solution and 4ml A phosphoric acid solution with a concentration of 0.61mol / l was heated up to 180°C, stirred for 12 hours, cooled to room temperature, filtered and washed with water, and the obtained solid product was dried at 110°C for 2 hours, and roasted at 550°C for 4 hours to obtain Phosphorus W / Al 2 o 3 catalyst.

[0029] To the phosphorus-containing W / Al 2 o 3 Add 4ml of nickel salt solution containing 0.7g of nickel nitrate hexahydrate into the solution, soak at room temperature for 14 hours, then dry at 110°C for 2 hours, and bake at 550°C for 4 hours to obtain phosphorus-containing NiW / Al 2 o 3 Hydrofining catalyst P2, the mass content and composition of the catalyst are listed in Table 1.

Embodiment 3

[0031] Weigh the molded Al 2 o 3 -SiO 2 Composite carrier (containing SiO 2 The weight percentage is about 10wt%) 5g, put it into a 100ml autoclave, add 0.3mol / l ammonium paratungstate solution 1.7ml, then add 2.4mol / l nitric acid 5.0ml, stir evenly, add 0.8mol / l lemon 13.4ml of acid solution and 5.1ml of ammonium hydrogen phosphate solution with a concentration of 0.61mol / l were heated up to 170°C, stirred and reacted for 16 hours, cooled to room temperature, the suspension was filtered and washed with water, and the obtained solid product was dried at 110°C for 2 Hours, calcination at 550°C for 4 hours to obtain phosphorus-containing W / Al 2 o 3 catalyst.

[0032] To the phosphorus-containing W / Al 2 o 3 Add 4ml of nickel salt solution containing 0.62g of nickel nitrate hexahydrate to the solution, soak at room temperature for 16 hours, then dry at 110°C for 2 hours, and bake at 550°C for 4 hours to obtain phosphorus-containing NiW / Al 2 o 3 Hydrofining catalyst P3, th...

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Abstract

The invention provides a method for preparing high-activity phosphoric hydrogenation refined catalyst capable of realizing deep desulfurization and denitrification. The method comprises the processes of loading VIB group metal active constituent and dip-loading VIII group metal active constituent by using hydro-thermal depositing method in the conditions that the inorganic acid is precipitating agent and the organic acid and phosphoric substance are composite dispersing agents. Compared with the catalyst with the same active constituent content and phosphorus content prepared by conventional dipping process, the phosphoric hydrogenation refined catalyst prepared by the method provided by the invention has higher desulfurization and denitrification activity, and is in particular applied todeep desulfurization and denitrification processing of diesel fuel.

Description

technical field [0001] The invention belongs to the technical field of preparation of hydrorefining catalysts, and in particular relates to a method for preparing a phosphorus-containing hydrorefining catalyst capable of achieving higher desulfurization and denitrogenation effects. Background technique [0002] Hydrofining technology is the most important means to produce low-sulfur and low-nitrogen clean diesel oil, and hydrofining catalyst is the core of hydrofining process. The supported catalyst with Group VIB metal W or Mo as the main agent, Group VIII metal Ni or Co as the auxiliary agent, and alumina as the carrier is currently the most widely used hydrofining catalyst. On this basis, there have been many studies and reports on introducing phosphorus into the catalyst as a promoter to improve the hydrogenation performance of the catalyst. [0003] Traditional supported hydrofining catalysts are mainly prepared by impregnation method, that is, the carrier is impregnat...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/188B01J27/19B01J37/10B01J37/02C10G45/08
Inventor 范煜鲍晓军王豪石冈刘海燕
Owner CHINA UNIV OF PETROLEUM (BEIJING)