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Hierarchical pore HZSM-5 zeolite molecular sieve

A zeolite molecular sieve and multi-stage pore technology, which is applied in the direction of molecular sieve catalysts, molecular sieves and alkali exchange compounds, crystalline aluminosilicate zeolites, etc., can solve the problems of uncontrollable pore structure, low yield of aromatic hydrocarbons, high yield of aromatic hydrocarbons, etc.

Active Publication Date: 2020-07-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In order to solve the problems in the prior art that the pore structure of hierarchical pore ZSM-5 is uncontrollable, the utilization rate of effective active sites is low, and the yield of aromatic hydrocarbons produced by cellulose catalytic pyrolysis is not high, the present invention intends to provide a biomass catalytic pyrolysis A catalyst for the preparation of aromatic hydrocarbons, which has a regular MFI framework structure, a hierarchical porous structure composed of micropores and non-penetrating mesopores, and has a high yield of aromatic hydrocarbons in catalytic pyrolysis of cellulose

Method used

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  • Hierarchical pore HZSM-5 zeolite molecular sieve
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  • Hierarchical pore HZSM-5 zeolite molecular sieve

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Catalyst preparation:

[0046] (1) 10 g of commercial ZSM-5 molecular sieve (SiO 2 / Al 2 o 3 =38) After roasting in a muffle furnace at 550°C for 5h, mix it with 300mL NaOH solution with a concentration of 0.1mol / L, and reflux and stir in an oil bath at 60°C for 1h; separate the reaction mixture from solid to liquid, and use deionized After fully washing with water, the separated solid was dried at 110°C for 12 hours to obtain solid A;

[0047] (2) Mix the molecular sieve obtained in step (1) with 300 mL of HCl solution with a concentration of 0.1 mol / L, and reflux and stir in an oil bath at 60°C for 1 hour; , drying the separated solid at 110°C for 12h to obtain solid B;

[0048] (3) Dissolve 1g of solid B, 0.16g of sodium metaaluminate, and 4.88g of tetrapropylammonium hydroxide (25% aqueous solution) in 13.5g of water, then add dropwise 6.25g of ethyl orthosilicate, and mix and prepare at room temperature The aqueous precursor solution of molecular sieves was st...

Embodiment 2

[0053] According to Example 1, only the alkali solution is changed to NaOH solution with a concentration of 0.5mol / L, and the oil bath is refluxed and stirred for 4 hours at 80°C, and only the acid solution is changed to an HCl solution with a concentration of 0.5mol / L, and the oil bath is heated at 80°C After reflux and stirring for 4 hours, only the crystallization time was changed for 72 hours, and other conditions remained unchanged, a hierarchically porous HZSM-5 zeolite molecular sieve was obtained, denoted as BA2.

[0054] The aromatics yield of cellulose pyrolysis catalyzed by the hierarchically porous HZSM-5 zeolite molecular sieve prepared in this example was 37.4%, and the coke yield was 32.7%.

Embodiment 3

[0056] According to Example 1, only the alkali solution is changed to NaOH solution with a concentration of 1.0mol / L, and the oil bath is refluxed and stirred for 8 hours at 100°C, and only the acid solution is changed to an HCl solution with a concentration of 1.0mol / L. Refluxing and stirring for 8 hours, only changing the crystallization time for 96 hours, and keeping other conditions unchanged, a hierarchically porous HZSM-5 zeolite molecular sieve was obtained, denoted as BA3.

[0057] The aromatics yield of cellulose pyrolysis catalyzed by the hierarchically porous HZSM-5 zeolite molecular sieve prepared in this example was 43.7%, and the coke yield was 26.1%.

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Abstract

The invention discloses a hierarchical pore HZSM-5 zeolite molecular sieve. The preparation method comprises the following steps: roasting ZSM-5 molecular sieve raw powder, mixing the ZSM-5 molecularsieve raw powder with alkali liquor for reaction, mixing the reaction product with acid liquor for reaction, and supplementing a silicon source, an aluminum source and organic alkali for hydrothermalsynthesis; performing separation, washing, drying and roasting treatment, performing ion exchange with an ammonium salt solution, and finally drying and roasting the product to obtain the ZSM-5 molecular sieve. The molecular sieve prepared by the invention has a regular MFI skeleton structure; a regular and controllable micro-mesopore hierarchical pore structure can be generated by secondary crystallization; meanwhile, a non-penetrability mesoporous structure is introduced; the advantages of a microporous ZSM-5 molecular sieve and a mesoporous material are combined; macromolecules generated inthe biomass catalytic thermal cracking process can easily enter and stay at the active sites of the molecular sieve, the diffusion path is shortened, the diffusion resistance of reactant molecules and product molecules in pore channels is reduced, and the contact probability of the reactant molecules and the active sites is increased, so that the aromatic hydrocarbon carbon yield is increased, and coke generation is reduced.

Description

technical field [0001] The invention relates to a multi-stage pore HZSM-5 zeolite molecular sieve, in particular to the preparation of a molecular sieve catalyst used to prepare aromatic hydrocarbons by catalytic thermal cracking of biomass, and belongs to the technical field of biomass energy utilization. Background technique [0002] Aromatics can be used not only as high-octane components in gasoline, but also as important basic raw materials for the production of bulk petrochemical products, and are in huge demand. At present, the production of aromatics at home and abroad mainly relies on petroleum resources, which are obtained through hydrogenation, reforming, aromatics conversion, separation and other processes under the conditions of catalysts and high temperature and high pressure. The process is complicated, and a large amount of exhaust gas is emitted, polluting the environment. [0003] Biomass is a renewable and clean energy source, and the preparation of aromat...

Claims

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Application Information

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IPC IPC(8): C01B39/38B01J29/40B01J35/10C10G11/05
CPCC01B39/38C01B39/026B01J29/40C10G11/05C01P2006/16C01P2002/72C01P2004/03C01P2006/17C01P2006/12C01P2006/14B01J35/615B01J35/633Y02P30/20
Inventor 马会霞周峰乔凯
Owner CHINA PETROLEUM & CHEM CORP