Light cycle oil hydrocracking catalyst and preparation method thereof

A technology for hydrocracking and light cycle oil, which is applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc. It can solve the problems of low cracking activity and poor nitrogen resistance, and achieve improved nitrogen resistance and cracking The effect of activity, reducing toxicity, and saving start-up time

Inactive Publication Date: 2017-04-26
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] One of the technical problems to be solved by the present invention is to provide a new catalyst for light cycle oil hydrocracking in o

Method used

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  • Light cycle oil hydrocracking catalyst and preparation method thereof
  • Light cycle oil hydrocracking catalyst and preparation method thereof
  • Light cycle oil hydrocracking catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0033] [Example 1]

[0034] The dry basis of 40g, 30g, 10g of USY zeolite (purchased from Zibo, Shandong, silicon-alumina ratio of 10), amorphous silica-alumina (purchased from Zibo, Shandong) and pseudo-boehmite (purchased from Zibo, Shandong) were added to the mixer. To homogeneity, then add 3g scallop powder, 5g volume ratio 1:1HNO to the mixture 3 The solution and 40 g of deionized water were ground into a dough suitable for extrusion. It was extruded through a die into a slender cylindrical shape (1.7 mm in diameter), dried at 120°C and then calcined at 550°C for 4 hours, and then cut into carrier particles with the same size for use (1.7×4.0mm).

[0035] The carrier particles are impregnated with a solution containing ammonium tetrathiomolybdate and ammonium tetrathiotungstate at 40°C, and the content of molybdenum sulfide and tungsten sulfide in the dipping solution is 5% and 9% of the dry weight of the carrier, After aging for 8 hours and drying, the carrier particles w

Example Embodiment

[0037] [Example 2]

[0038] The dry basis of 40g, 30g, 10g of USY zeolite (purchased from Zibo, Shandong, silicon-alumina ratio of 10), amorphous silica-alumina (purchased from Zibo, Shandong) and pseudo-boehmite (purchased from Zibo, Shandong) were added to the mixer. To homogeneity, then add 3g scallop powder, 5g volume ratio 1:1HNO to the mixture 3The solution and 40 g of deionized water were ground into a dough suitable for extrusion. It was extruded through a die into a slender cylindrical shape (1.7 mm in diameter), dried at 120°C and then calcined at 550°C for 4 hours, and then cut into carrier particles with the same size for use (1.7×4.0mm).

[0039] The carrier particles are impregnated with a solution containing ammonium tetrathiomolybdate and ammonium tetrathiotungstate at 40°C, and the content of molybdenum sulfide and tungsten sulfide in the dipping solution is 5% and 9% of the dry weight of the carrier, After aging for 8 hours and drying, the carrier particles we

Example Embodiment

[0041] [Example 3]

[0042] Beta zeolite (purchased from Zibo, Shandong, with a silicon-to-aluminum ratio of 13), amorphous silica-alumina (purchased from Zibo, Shandong) and pseudo-boehmite (purchased from Zibo, Shandong) were added to the mixer on a dry basis, respectively. To homogeneity, then add 3g scallop powder, 5g volume ratio 1:1HNO to the mixture 3 The solution and 40 g of deionized water were ground into a dough suitable for extrusion. It was extruded through a die into a slender cylindrical shape (1.7 mm in diameter), dried at 120°C and then calcined at 550°C for 4 hours, and then cut into carrier particles with the same size for use (1.7×4.0mm).

[0043] The carrier particles are impregnated with a solution containing ammonium tetrathiomolybdate and ammonium tetrathiotungstate at 40°C, and the content of molybdenum sulfide and tungsten sulfide in the dipping solution is 5% and 9% of the dry weight of the carrier, After aging for 8 hours and drying, the carrier part

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Abstract

The invention relates to a light cycle oil hydrocracking catalyst and a preparation method thereof. The problems of low light cycle oil cracking activity and poor nitrogen resistance of traditional hydrocracking catalysts are mainly solved in the invention. The catalyst comprises, by weight, 15-35% of at least one of FAU zeolite, BEA zeolite and MFI zeolite, 5-16% of amorphous silica-alumina, 10-20% of pseudo-boehmite, 5-10% of molybdenum sulfide, 9-16% of tungsten sulfide and 3-6% of at least one active component selected from nickel phosphate and cobalt phosphate. The light cycle oil hydrocracking catalyst adopting the above technical scheme well solves the problems, has the advantages of no precurng, high cracking activity, high nitrogen resistance, and flexible and controllable product distribution, and can be used in the field of hydrogenation refining and chemical engineering.

Description

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Claims

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Application Information

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Owner CHINA PETROLEUM & CHEM CORP
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