Hierarchical structure ZSM-5 molecular sieve containing lanthanum and nickel or/and zinc , and preparation method and application thereof

A ZSM-5, molecular sieve technology, applied in the field of catalytic materials and catalytic chemistry, can solve the problems of increasing gel concentration, difficulty in synthesis, great challenges, etc., and achieves the effects of good test repeatability, simple operation and pollution reduction.

Pending Publication Date: 2021-06-29
PETROCHINA CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This is mainly because ZSM-5 molecular sieve with low silicon-aluminum ratio is mainly used in olefin aromatization reaction, and it is very difficult to synthesize pure ZSM-5 zeolite molecular sieve with low silicon-aluminum ratio by liquid phase hydrothermal synthesis
If one or more metal salts are added, the gel concentration will be further increased, making the synthesis more difficult
Therefore, although the hydrothermal synthesis of zinc, nickel, lanthanum and low-silicon ZSM-5 molecular sieves with a multi-level structure is of great significance, the synthesis is more challenging, and there have been no relevant patent reports so far.

Method used

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  • Hierarchical structure ZSM-5 molecular sieve containing lanthanum and nickel or/and zinc , and preparation method and application thereof
  • Hierarchical structure ZSM-5 molecular sieve containing lanthanum and nickel or/and zinc , and preparation method and application thereof
  • Hierarchical structure ZSM-5 molecular sieve containing lanthanum and nickel or/and zinc , and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0063] Example 1: Preparation of ZSM-5 zeolite molecular sieve with zinc and lanthanum hierarchical structure

[0064](1) Treatment of silicon source:

[0065] Take 2g of tetrapropylammonium bromide (0.0075mol, equivalent to 0.06 times that of coarse-pored silica gel) at 25°C, add it to 10g of water (0.556mol, equivalent to 4.444 times that of coarse-pored silica gel), stir evenly, and then add 7.5g Coarse-porous silica gel (0.125 mol), and continue to stir for about 30 minutes to obtain a silicon source solution.

[0066] (2) Treatment of aluminum source, zinc source and lanthanum source:

[0067] At 25°C, add 0.57g of sodium metaaluminate (0.0025mol, equivalent to 0.02 times that of coarse-pored silica gel) into 8.75g of water (0.486mol, equivalent to 3.889 times that of coarse-pored silica gel), stir for 5 minutes and then add 1.47g Zinc nitrate hexahydrate (0.0049mol, equivalent to 0.04 times of coarse-pore silica gel), add 0.57g lanthanum chloride (0.0014mol, equivalent...

Embodiment 2

[0072] Embodiment 2: the preparation of nickel, lanthanum multi-level structure ZSM-5 zeolite molecular sieve

[0073] (1) Treatment of silicon source and nickel source:

[0074] At 25°C, take 3g of tetrapropylammonium bromide (0.0113mol, equivalent to 0.09 times of white carbon black) and add it to 10g of water (0.556mol, equivalent to 4.444 times of white carbon black) and stir evenly, then add 7.5g White carbon black (0.125mol) and 0.93g nickel nitrate hexahydrate (0.0032mol, equivalent to 0.026 times of white carbon black), continue stirring for about 30min to obtain silicon source and nickel source solutions, and then aged at 50°C for 10 hours to obtain a uniform solution.

[0075] (2) Treatment of aluminum source and lanthanum source:

[0076] At 25°C, add 1.02g of aluminum isopropoxide (0.0025mol, equivalent to 0.02 times of white carbon black) to 8.75g of water (0.486mol, equivalent to 3.889 times of white carbon black), add 0.29g of lanthanum chloride (0.0007mol, e...

Embodiment 3

[0081] Example 3: Preparation of ZSM-5 Zeolite Molecular Sieve with Zinc, Nickel, Lanthanum and Low Silicon Hierarchical Structure

[0082] (1) Treatment of silicon source and nickel source:

[0083] Take 3g of tetrapropylammonium bromide (0.0188mol, equivalent to 0.15 times of coarse-pore silica gel) at 30°C and add them to 10g of water (0.556mol, equivalent to 4.444 times of coarse-pore silica gel) and stir evenly, then add 7.5g Coarse porous silica gel (0.125mol) and 0.41g nickel nitrate hexahydrate (0.0014mol, equivalent to 0.011 times of coarse porous silica gel), continue to stir for about 30min to obtain silicon source and nickel source solutions, and then aged at 90°C for 2 hours to obtain a uniform solution.

[0084] (2) Treatment of aluminum source, zinc source and lanthanum source:

[0085] Add 1.02g of aluminum isopropoxide (0.0025mol, equivalent to 0.02 times that of coarse-pored silica gel) at 30°C to 8.75g of water (0.486mol, equivalent to 3.889 times that of ...

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Abstract

The invention relates to a hierarchical structure ZSM-5 molecular sieve containing lanthanum and nickel or / and zinc, a preparation method thereof, and application of the hierarchical structure ZSM-5 molecular sieve in catalytic gasoline olefin reduction. The molecular sieve is ZSM-5 zeolite which is obtained by adopting a hydrothermal synthesis method and has a silicon-aluminum atomic ratio of 10-50, and pores in the zeolite contain lanthanum and zinc or / and nickel; the hierarchical structure ZSM-5 molecular sieve has a mesoporous structure formed by secondary accumulation of crystal grains of the molecular sieve, the volume of mesopores is not less than 0.09 cm<3> / g, the specific surface area is greater than 200 cm<2> / g, the size of primary particles of the molecular sieve is about 300 nm to 2 [mu]m, and the size of secondary accumulation particles is 2 [mu]m to 8 [mu]m. The hierarchical structure ZSM-5 molecular sieve containing lanthanum and nickel or / and zinc has high acid content and L acid / B acid ratio, and more mesoporous structures improve the diffusion rate of macromolecular reactants or products and enhance the carbon containing capacity of the catalyst, so the hierarchical structure ZSM-5 molecular sieve has high desulfurization and olefin reduction-octane number recovery activity and long-period stability in catalytic gasoline olefin reduction-modification reaction.

Description

technical field [0001] The invention belongs to the technical field of catalytic materials and catalytic chemistry, and specifically relates to a hydrothermal synthesis method and application of a gasoline-reduced olefin-modified multi-stage structure ZSM-5 zeolite molecular sieve. Background technique [0002] Due to its unique pore structure, acid properties, high hydrothermal stability, and lipophilic and hydrophobic properties, ZSM-5 molecular sieve itself is a good catalyst and is often used as a solid acid catalyst. It is widely used in alkylation, catalytic cracking, alcohol, etc. reactions such as dehydration. At the same time, because of its high specific surface area and excellent ion exchange performance, it is also an excellent carrier for catalytically active metal ions or metal compounds. ZSM-5 molecular sieve-loaded iron, silver, copper and other catalysts are used in the oxidation of benzene and nitrogen oxides. It exhibits excellent catalytic performance in...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/46B01J29/40B01J37/10B01J35/10C01B39/40C10G45/12C10G45/64
CPCB01J29/46B01J29/405B01J37/10B01J37/0018B01J35/1095B01J35/1014B01J35/1019B01J35/1038C01B39/40C10G45/12C10G45/64B01J2229/18C01P2006/14C01P2006/12C01P2004/62C01P2004/61
Inventor 鞠雅娜李天舒兰玲吴志杰葛少辉胡亚琼赵秦峰张然吕忠武冯琪
Owner PETROCHINA CO LTD
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