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Aromatization catalyst as well as preparation method and application thereof

An aromatization and catalyst technology, which is applied in the field of aromatization catalyst and its preparation, can solve the problem that the selectivity of aromatic hydrocarbons needs to be further improved, and achieves the effect of delaying the carbon deposition rate, reducing the influence of diffusion resistance and improving the selectivity.

Active Publication Date: 2020-05-15
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there are still some problems with gallium-modified ZSM-5 molecular sieve catalysts. For example, the selectivity of aromatics needs to be further improved, and the service life and thermal stability of the catalyst need to be further improved.

Method used

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  • Aromatization catalyst as well as preparation method and application thereof
  • Aromatization catalyst as well as preparation method and application thereof
  • Aromatization catalyst as well as preparation method and application thereof

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preparation example Construction

[0040] The present invention provides a method for preparing an aromatization catalyst described in the above technical scheme, comprising the following steps:

[0041] (1) adding the silicon source to the mixed aqueous solution including the aluminum source and the directing agent, performing a hydrothermal reaction, and roasting the solid product of the hydrothermal reaction to obtain the ZSM-5 molecular sieve matrix;

[0042] (2) mixing the ZSM-5 molecular sieve parent body, water and directing agent, and roasting the gained solid product after hydrothermal treatment;

[0043] (3) performing alkali treatment on the product obtained by roasting the step (2) to obtain a hierarchically porous ZSM-5 molecular sieve;

[0044] (4) the ZSM-5 molecular sieve of described multi-stage hole is carried out ammonium ion modification, obtains modified ZSM-5 molecular sieve after roasting;

[0045] (5) ion-exchange the modified ZSM-5 molecular sieve with the gallium salt solution, and ob...

Embodiment 1

[0078] (1) Weigh 0.1822g sodium metaaluminate and place it in a beaker, add 38.75g deionized water, 20.336g mass fraction of 25% tetrapropylammonium hydroxide aqueous solution and 0.1g sodium hydroxide, stir until the solution is clear, Then slowly add 20.833g tetraethyl orthosilicate dropwise, and after stirring for 12 hours, transfer the solution into a hydrothermal reaction kettle, crystallize at 170°C for 4 days, remove the mother liquor by centrifugation, wash with deionized water until the solution becomes neutral, Dry overnight at 100°C, and calcine at 600°C for 10 hours to obtain the ZSM-5 molecular sieve precursor;

[0079] (2) Grind the prepared ZSM-5 molecular sieve precursor into powder, weigh 1gZSM-5 molecular sieve precursor (0.4g silicon content), 0.01g sodium hydroxide and 0.002g sodium metaaluminate and disperse them in 5mL water and 3mL of 1mol / L tetrapropylammonium hydroxide solution, stirred for 10 minutes, then transferred to a hydrothermal reaction kettle...

Embodiment 2

[0085] Prepare the aromatization catalyst according to the steps of Example 1, the difference is that the quality of sodium metaaluminate in Example 1 is replaced by 0.3279g, sodium hydroxide is replaced by sodium carbonate, the alkali treatment time is 6h, and other conditions are not changed. Change, the obtained sample is recorded as catalyst 2#.

[0086] The JEM2100-F field emission transmission electron microscope produced by Rigaku Corporation of Japan is used to observe catalyst 2#, and the results are as follows figure 2 shown. figure 2 It is shown that the catalyst has a hierarchical porous structure of micropores, mesopores and macropores, indicating that the molecular sieve synthesized by the present invention is indeed a hierarchical porous structure.

[0087] Carry out BET adsorption on catalyst 2#, the obtained isotherm adsorption curve is as follows image 3 shown. image 3 It shows that the BET specific surface of catalyst 2# is 392m 2 / g, the pore volume...

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Abstract

The invention provides an aromatization catalyst as well as a preparation method and application thereof, and belongs to the technical field of catalysts. The aromatization catalyst comprises an inorganic oxide and a modified Ga / ZSM-5 molecular sieve; the modified Ga / ZSM-5 molecular sieve comprises a modified ZSM-5 molecular sieve and Ga loaded on pore channels and / or the surface of the modified ZSM-5 molecular sieve, and the modified ZSM-5 molecular sieve has a hierarchical pore structure of micropores, mesopores and macropores. The modified ZSM-5 molecular sieve in the aromatization catalysthas the hierarchical porous structure of micropores, mesopores and macropores, can reduce the influence of diffusion resistance in aromatization reaction, delays the carbon deposition rate, greatly improves the activity, selectivity and stability of the catalyst, and prolongs the service life of the catalyst. The catalyst is used for catalyzing the aromatization reaction of propane, the catalystshows quite high stability, the regeneration service life can reach 320 h or longer, and the selectivity of aromatic hydrocarbon can reach 73.3%.

Description

technical field [0001] The invention relates to the technical field of catalysts, in particular to an aromatization catalyst and its preparation method and application. Background technique [0002] Aromatics is an important basic raw material of organic chemical industry. At present, the annual consumption of aromatics in my country is huge. The conversion of abundant and cheap low-carbon hydrocarbon components into high value-added benzene, toluene, and xylene has become an important research hotspot in the past 30 years. [0003] Catalysts commonly used in the aromatization of low-carbon hydrocarbons are generally metal-supported catalysts (such as Pt / Al 2 o 3 、Cr 2 o 3 / Al 2 o 3 etc.) and molecular sieve catalysts (such as MFI type, MCM series, L molecular sieve, etc.). At present, the most researched molecular sieve catalyst is ZSM-5 molecular sieve catalyst. [0004] Patent CN1938245N discloses a Pt / Ga-ZSM-5 molecular sieve catalyst with MFI structure, which ca...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/40B01J35/10C07C2/76C07C15/04C07C15/06C07C15/08
CPCB01J29/405C07C2/76B01J2229/186B01J2229/42C07C2529/40B01J35/394B01J35/64B01J35/633B01J35/647B01J35/615C07C15/04C07C15/06C07C15/08Y02P20/52B01J2229/38B01J23/18B01J37/04B01J37/082B01J2229/183C07C2/84C07C2/06C07C2/08C07C2/10C07C2/04C07C2/12B01J35/392B01J35/643B01J35/651B01J35/653B01J35/657B01J35/695
Inventor 樊卫斌石德志朱华青董梅王建国吴志伟焦卫勇刘俊义王东飞栗进波崔艳斌张一波
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI