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Hydrocracking catalyst and preparation method thereof

A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, hydrocarbon cracking to produce hydrocarbons, etc. , pore volume and small pore size, etc., to achieve the effect of good catalytic performance, good acid function and uniform dispersion

Active Publication Date: 2013-05-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the catalyst containing cesium phosphotungstate salt has good hydrocracking reaction activity, due to the strong acidity of phosphotungstic acid, after adding it in the catalyst preparation process, it has a great impact on the formation of carrier silicon oxide. When the cesium phosphotungstate content is high, the specific surface area, pore volume and pore diameter of the catalyst are relatively small, which affects the hydrocracking reaction activity of the catalyst

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Mix 45 ml of cesium carbonate solution with a concentration of 0.1 g / ml, 31 ml of nickel nitrate solution with a concentration of 1 g / ml and 26 ml of tartaric acid solution with a concentration of 1 g / ml to prepare mixed solution A, and stir at room temperature for 0.5 h ; At the same time, 72 ml of lauric acid solution with a concentration of 1 g / ml was mixed with 144 g of silica sol to obtain mixed solution B, which was stirred at room temperature for 0.5 h; then solution A and solution B were mixed, stirred for 0.5 h, and then added 42 g of silicotungstic acid aqueous solution, stirred at 80°C to evaporate the solution to dryness, dried the resulting solid for 8 h, and calcined at 400°C for 4 h to obtain Ni-Cs 2 h 2 SiW 12 o 40 / SiO 2 Catalyst, wherein nickel content is 10wt%, Cs 2 h 2 SiW 12 o 40 The content is 40wt%, the molar ratio of tartaric acid to nickel is 1, and the molar ratio of lauric acid to silicon oxide is 0.5. The physicochemical properties of...

Embodiment 2

[0027] Mix 71 ml of cesium carbonate solution with a concentration of 0.1 g / ml, 25 ml of nickel nitrate solution with a concentration of 1 g / ml and 31 ml of tartaric acid solution with a concentration of 1 g / ml to prepare mixed solution A, and stir at room temperature for 0.5 h ; At the same time, 79 ml of lauric acid solution with a concentration of 1 g / ml was mixed with 112 g of silica sol to obtain mixed solution B, which was stirred at room temperature for 0.5 h; then solution A and solution B were mixed, stirred for 0.5 h, and then added 52 g of silicotungstic acid aqueous solution, stirred at 80°C to evaporate the solution to dryness, dried the resulting solid for 8 h, and calcined at 400°C for 4 h to obtain Ni-Cs 2.5 h 1.5 SiW 12 o 40 / SiO 2 Catalyst, wherein nickel content is 8wt%, Cs 2.5 h 1.5 SiW 12 o 40 The content is 50wt%, the molar ratio of tartaric acid to nickel is 1.5, and the molar ratio of lauric acid to silicon oxide is 0.7. The physicochemical prop...

Embodiment 3

[0030] Mix 25 ml of cesium carbonate solution with a concentration of 0.1 g / ml, 47 ml of nickel nitrate solution with a concentration of 1 g / ml and 19 ml of tartaric acid solution with a concentration of 1 g / ml to prepare mixed solution A, and stir at room temperature for 0.5 h ; At the same time, 49 ml of lauric acid solution with a concentration of 1 g / ml was mixed with 162 g of silica sol to obtain mixed solution B, which was stirred at room temperature for 0.5 h; then solution A and solution B were mixed, stirred for 0.5 h, and then added 31 g of silicotungstic acid aqueous solution, stirred at 80°C to evaporate the solution to dryness, dried the resulting solid for 8 h, and calcined at 400°C for 4 h to obtain Ni-Cs 2.5 h 1.5 SiW 12 o 40 / SiO 2 Catalyst, wherein nickel content is 15wt%, Cs 1.5 h 2.5 SiW 12 o 40 The content is 30wt%, the molar ratio of tartaric acid to nickel is 0.5, and the molar ratio of lauric acid to silicon oxide is 0.3. The physicochemical pro...

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Abstract

The invention discloses a hydrocracking catalyst and a preparation method thereof. In the catalyst, the acidic component is a silicotungstate, the hydrogenation metal component is nickel, and the carrier is silicon oxide. The catalyst is prepared by: adding a nickel salt and an alkali metal salt respectively into an aqueous solution containing organic acid I to obtain a solution A, adding a silicon source into a solution containing organic acid II to obtain a solution B, then mixing the solution A with the solution B, adding a silicotungstic acid aqueous solution, conducting stirring to evaporate the solution, and carrying out drying and roasting, thus obtaining the catalyst. The heteropolyacid used by the method is silicotungstic acid, and two organic acids are used cooperatively to reach a mutual promotion effect, so that the metal components and the acidic component are dispersed more evenly, the hydrogenation activity and the acid function are matched better, and also the catalyst can have larger specific surface area, pore size and pore volume. Thus, the catalyst has better catalytic performance. The catalyst prepared by the invention is especially suitable for a hydrocracking reaction of long chain alkane.

Description

technical field [0001] The invention relates to a hydrocracking catalyst and a preparation method thereof, in particular to a long-chain alkane hydrocracking catalyst free of presulfurization and high activity and a preparation method thereof. Background technique [0002] In the oil refining industry, hydrocracking is an important process for producing high-quality light oil products from heavy oil. A transformation process of chemical reactions such as rearrangement and cleavage. The hydrocracking process can not only produce high-quality light oil products, but also has a high yield of liquid phase products. The core of its technology is the catalyst. The hydrocracking catalyst is a dual-function catalyst, which has both the acid function and the hydrogenation function. The acid function of the hydrocracking catalyst involved in US 5,536,687, US 5,447,623 and EP0028938A1 is mainly provided by molecular sieves, and the hydrogenation component is selected from Mo-Ni or W-...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/888B01J35/10C07C4/06
CPCY02P20/52
Inventor 金浩孙素华刘杰朱慧红杨光
Owner CHINA PETROLEUM & CHEM CORP
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