Preparation method for hydrocracking catalyst

A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems such as insufficient catalyst stability and unstable properties of heteropolyacids

Active Publication Date: 2013-02-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the properties of heteropolyacids are unstable, and they will gradually decompose and

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Prepare an impregnation solution with a weight concentration of 30% ammonium dihydrogen phosphate, tungsten and nickel, impregnate the carrier T-1 of Comparative Example 1 with the prepared impregnation solution for 2 hours, dry at 120°C for 4 hours, and dry at 120°C for 4 hours. Heat treatment at ℃ for 6 hours, and then reductive activation under hydrogen atmosphere. The reductive activation program is to rise from room temperature to 450°C at a rate of 5°C / min, and to rise from 450°C to 700°C at a heating rate of 2°C / min. The catalyst C-1 of the present invention was prepared by keeping the temperature at 700°C for 2 hours.

Embodiment 2

[0042] Prepare an impregnating solution with a weight concentration of 40% ammonium dihydrogen phosphate and containing tungsten and nickel, impregnate the carrier T-2 of Comparative Example 2 with the prepared impregnating solution for 2 hours, dry at 100°C for 6 hours, and place in an air atmosphere Heat treatment at 400°C for 1 hour, and then perform hydrogen activation under a hydrogen atmosphere. Firstly, heat up from room temperature to 350°C at a rate of 10°C / min, then rise from 350°C to 600°C at a rate of 1°C / min. The temperature was kept at 600° C. for 4 hours to prepare the phosphating transition metal catalyst C-2.

Embodiment 3

[0047] Prepare an impregnating solution with a weight concentration of 40% ammonium hydrogen phosphate and tungsten and nickel, impregnate the carrier T-3 of Comparative Example 3 with the prepared impregnating solution for 2 hours, dry at 110°C for 6 hours, and dry at 350 °C in an air atmosphere. Heat treatment at ℃ for 2 hours, and then under hydrogen atmosphere, conduct activation treatment, firstly increase from room temperature to 450 ℃ at 8 ℃ / min, increase from 450 ℃ to 650 ℃ at a heating rate of 1 ℃ / min, and at 650 °C for 4 hours to prepare the phosphating transition metal catalyst C-3.

[0048] Table 1 Physicochemical properties of catalyst supports.

[0049] Numbering T-1 T-2 T-3 Molecular sieve, wt% 12.0 7.0 4.0 Amorphous silica-alumina, wt% 25.0 53.0 30.0 Macroporous alumina, wt% 43.0 20.0 46.0 Binder, wt% 20.0 20.0 20.0 Pore ​​volume, ml / g 0.73 0.76 0.78 Specific surface area, m 2 / g 425 392 383

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Abstract

The invention describes a preparation method for a hydrocracking catalyst. The method comprises the following steps of (1) preparing a catalyst carrier containing a molecular sieve and an inorganic refractory oxide; (2) preparing a dipping solution containing a VIB group metallic compound, a VIII group metallic compound and an inorganic phosphorous-containing compound; (3) dipping the catalyst carrier obtained from the step (1) with the dipping solution prepared by the step (2), and then drying the dipped material; (4) performing heat treatment on the material obtained from the step (3) in an air atmosphere; and (5) performing hydrogen activation on the material obtained from the step (4), and obtaining the hydrocracking catalyst used for hydrocracking reactions after the activation. The hydrocracking catalyst prepared by the method has outstanding usage performance, and is particularly suitable for a hydrocracking process of increasing middle distillates.

Description

technical field [0001] The invention relates to a method for preparing a hydrocracking catalyst. The catalyst has excellent hydrocracking performance, high activity and high selectivity for medium oil. Background technique [0002] The hydrocracking catalyst is a dual-functional catalyst with hydrogenation and cracking properties. Non-precious metal hydrocracking catalysts generally use Group VIB and Group VIII metals as hydrogenation components, and the cracking performance is mainly provided by acidic components. Crystalline zeolite and / or amorphous silica-alumina can be used. Simple use of amorphous silica-alumina, although the selectivity is high, but the activity is low, and the flexibility of operation is limited. In most hydrocracking catalysts, crystalline zeolite is used as the acidic component, or crystalline zeolite and amorphous Silica and aluminum are common acidic components. [0003] Most of the medium-oil hydrocracking catalysts currently used in industrial...

Claims

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Application Information

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IPC IPC(8): B01J29/16B01J29/78C10G47/20
Inventor 谷明镝黄薇
Owner CHINA PETROLEUM & CHEM CORP
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