Composite mesoporous molecular sieve hydrocracking catalyst and uses thereof

A mesoporous molecular sieve and composite molecular sieve technology, applied in the field of composite mesoporous molecular sieve hydrocracking catalysts, can solve the problems of high acidity, low medium oil selectivity and unfavorable medium oil selectivity of β molecular sieve, and achieve high aromatic potential and low BMCI value Effect

Active Publication Date: 2008-09-24
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] CN1393521A discloses medium oil type hydrocracking catalyst with amorphous silicon aluminum, gamma and β compound molecular sieve as carrier, and the acidity of β molecular sieve is high, which is unfavorable for the improvement of medium oil selectivity, medium oil selectivity is 66%~69%, medium oil selectivity Relatively low
The initial reaction temperature of the catalyst is 404°C-406°C, the selectivity of medium oil is 78%-79%, and the cracking activity of the catalyst is low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Synthesis of AlSBA-15 / HY(9∶1) Composite Molecular Sieve

[0035] Add 50g of P123 dissolved in 2000ml of 0.03M hydrochloric acid solution, stir and dissolve at 50°C for 1hr, then add 5.1g of aluminum isopropoxide and 3.4g of NH with a Si / Al ratio of 10 4 Y zeolite, continue to stir at 40°C for 20hrs, then add 104g of tetraethyl orthosilicate, continue to stir for 48hrs, then place the mixture in a hydrothermal kettle at 100°C and continue to react for 24hrs, then filter and wash to obtain a solid, which is roasted at 550°C to obtain AlSBA The composite molecular sieve material with a weight ratio of -15 and HY of 9:1, referred to as AlSBA-15 / HY (9:1) composite molecular sieve, is numbered A.

Embodiment 2

[0037] Synthesis of AlSBA-15 / HY(3∶1) Composite Molecular Sieve

[0038] Add 80g of P123 dissolved in 4800ml of 0.03M hydrochloric acid solution, stir and dissolve at 60°C for 1hr, then add 8.2g of aluminum isopropoxide and 16g of NH with a Si / Al ratio of 15 4 Y zeolite, continue to stir at 40°C for 20hrs, then add 166g of tetraethyl orthosilicate, continue to stir for 48hrs, then place the mixture in a hydrothermal kettle at 100°C and continue to react for 24hrs, then filter and wash to obtain a solid, which is roasted at 600°C to obtain AlSBA The composite molecular sieve material whose weight ratio of -15 and HY is 3:1 is referred to as AlSBA-15 / HY (3:1) composite molecular sieve, and its serial number is B.

Embodiment 3

[0040] Synthesis of AlSBA-15 / HY(1∶1) Composite Molecular Sieve

[0041] Add 50g of P123 dissolved in 2000ml of 0.03M hydrochloric acid solution, stir and dissolve at 40°C for 1hr, then add 5.1g of aluminum isopropoxide and 30g of NH with a Si / Al ratio of 7 4 Y zeolite, continue to stir at 40°C for 20hrs, then add 104g of tetraethyl orthosilicate, continue to stir for 48hrs, then place the mixture in a hydrothermal kettle at 100°C and continue to react for 24hrs, then filter and wash to obtain a solid, which is roasted at 520°C to obtain AlSBA The composite molecular sieve material whose weight ratio of -15 and HY is 1:1 is referred to as AlSBA-15 / HY (1:1) composite molecular sieve, and its code is C.

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Abstract

The invention relates to a composite mesoporous molecular sieve hydrocracking catalyst and the application thereof. The catalyst composed of following components of 20 to 50 percent of amorphous silica-alumina, 5 to 30 percent of alumina, 10 to 25 percent of adhesives, 10 to 40 percent of Group VIB-the metal oxides, 1 to 20 percent of Group VIII-the metal oxides, 0.1 to 10 percent of Group VA-the metal oxides, and 1 to 40 percent of composite mesoporous molecular sieve, wherein, the composite mesoporous molecular sieve is a composite molecular sieve composed of a mesoporous molecular sieve AlSBA-15 and/or AlSBA-15/Y; the weight ratio of the composite molecular sieve AlSBA-15/Y in the AlSBA-15 and a Y molecular sieve is 9:1 to 1:9; the weight ratio of the mesoporous molecular sieve and a pore molecular sieve is 3:1 to 1:3, the silica alumina ratio is 10:1 to 40:1, and the silica alumina ratio of the Y molecular sieve is 5:1to 20 :1. The catalyst used for hydrocracking for heavy oil shows high activity for hydrocracking and high medium oil selectivity.

Description

technical field [0001] The invention relates to a composite mesoporous molecular sieve hydrocracking catalyst and its application. Background technique [0002] In recent years, with the heavy and inferior quality of crude oil in the world, the hydrocracking process with strong adaptability to raw materials and good product quality has become one of the important means of lightening heavy oil. At the same time, worldwide demand for middle distillates continues to grow, and refineries are under increasing pressure to produce high-quality middle distillate products. Therefore, the medium oil hydrocracking process capable of producing high-quality clean fuels has been more and more widely used. As the core of hydrocracking technology, the development of CNPC hydrocracking catalyst is the key to the production of clean fuels. [0003] The hydrocracking catalyst is a dual-functional catalyst with hydrogenation and cracking functions, and is generally made of non-precious metals...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/80C10G45/12
Inventor 孙发民赵东元王刚张福强张学军于春梅戴宝琴马建英王甫村葛冬梅李凤铉张庆武李井泉王东青王铁庆李晓文孙举
Owner PETROCHINA CO LTD
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