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mo/hzsm-5 catalyst, preparation method and application thereof

A catalyst and template technology, applied in the field of catalysis, can solve the problems affecting the mechanical strength and stability of the catalyst, the decrease of crystallinity, the loss of Mo species, etc., to achieve good catalytic activity and stability, promote efficient generation, and improve dispersion. Effect

Active Publication Date: 2020-09-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, these complex operating techniques are not only inefficient, but also easily cause the loss of Mo species, or destroy the skeleton structure of the molecular sieve carrier, resulting in a decrease in crystallinity, which seriously affects the production of HZSM-5 and its Mo species. The mechanical strength and stability of the Mo / HZSM-5 catalyst are difficult to meet the technical requirements of the future long-term industrial application of the reaction catalyst

Method used

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  • mo/hzsm-5 catalyst, preparation method and application thereof
  • mo/hzsm-5 catalyst, preparation method and application thereof
  • mo/hzsm-5 catalyst, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Weigh 0.72g of molybdenum acetylacetonate, 12.5g of tetraethyl orthosilicate and 0.25g of aluminum isopropoxide, and add them into a beaker filled with a mixed organic solvent of 20mL of isopropanol and 20mL of toluene. Keep stirring in a water bath at 25°C for 3 hours. After all the materials are completely dissolved and fully mixed, a clear solution I is obtained; weigh 8g of tetrapropylammonium hydroxide, 17g of water and 10mL of isopropanol, mix and stir to form a uniform solution II.

[0027] Under continuous stirring conditions, use a peristaltic pump to slowly add solution II to solution I dropwise to configure a HZSM-5 molecular sieve synthesis solution, in which the molar ratio of silicon source, aluminum source, template agent, and water is 1:0.02:0.16:24. After continuing to stir for 0.5h, the temperature of the water bath was raised to 40-50°C, and the synthetic solution gradually turned into a transparent gel. After aging and natural air-drying, the xerogel ...

Embodiment 2

[0033] The synchrotron radiation method was used to characterize and analyze the Mo species placement and coordination states of catalysts A and B. figure 1 , figure 2 Catalyst A and catalyst Mo species L in the total electron (TEY) and fluorescence (FY) collection modes, respectively 3 -Edge near-edge absorption rate (XANES) changes. Through two different acquisition methods of TEY and FY, the coordination information of Mo species located in different regions of the bulk phase and the outer surface of the molecular sieve can be obtained.

[0034] Depend on figure 1 It can be seen that MoO with a typical hexacoordinated octahedral structure 3 Compared with the standard sample, both the four-coordinated Mo species and the hexa-coordinated Mo species exist on the outer surface of the catalyst A of Example 1 and the catalyst B of Comparative Example 1. In the normalized spectrogram, it can be seen from the peak intensity difference The content of Mo species on the outer sur...

Embodiment 3

[0037] Before carrying out the oxygen-free dehydrogenation aromatization of methane, the Mo / HZSM-5 catalysts prepared in Example 1 and Comparative Example 1 were pressed into tablets, crushed, and sieved into 20-60 meshes. Weigh 0.6g of catalyst A or catalyst B and load it into a stainless steel fixed-bed continuous flow reactor with an inner diameter of 7mm, and the ratio of bed height to diameter is 4. The reaction pressure is 1atm, the temperature of the catalyst is raised to 750°C in a He atmosphere of 30ml / min, and after stabilizing at this temperature for 30min, switch to 60ml / min raw material gas to start the reaction, and the space velocity is 6000ml / g cat h. Using the method of adding nitrogen to the feed gas as an internal standard (CH 4 / N 2 =9), the product is introduced into two gas chromatographs equipped with thermal conductivity detector and hydrogen flame detector respectively by two six-way valves and carried out on-line analysis, to investigate the convers...

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Abstract

The invention relates to an Mo / HZSM-5 catalyst as well as a preparation method and application thereof, belongs to the technical field of catalysis and mainly aims at solving the problem that the stability of the Mo / HZSM-5 catalyst is lowered in order to realize the high pore dispersion of Mo species in the prior art. The problem is better solved by adopting the technical scheme that the Mo / HZSM-5catalyst is prepared by one-step solid-phase crystal transition realized by simultaneously introducing a precursor of the Mo species or a second metal component Ag to a molecular sieve synthesis liquid in a process of synthesizing HZSM-5 by using a dry glue method. The Mo species in the Mo / HZSM-5 catalyst prepared by using the method disclosed by the invention is mainly selectively located insidea pore passage of a molecular sieve carrier in a tetra-coordinated structural state, so that the catalytic performance of methane dehydroaromatization of the catalyst is improved, and the Mo / HZSM-5 catalyst can be used for industrial application to methane dehydroaromatization.

Description

technical field [0001] The invention belongs to the technical field of catalysis, and in particular relates to a preparation method and application of a Mo / HZSM-5 catalyst. Background technique [0002] The well-established technologies for exploiting unconventional natural gas resources such as shale gas provide an important raw material guarantee for the large-scale chemical utilization of methane. In addition to preparing various chemical products through the indirect method of the synthesis gas platform, methane can also be directly converted into important chemical products such as aromatics and olefins through the chain growth reaction after activation by the catalyst. Under oxygen-free conditions, the anaerobic dehydroaromatization of methane can directly convert methane to benzene and hydrogen with high atom economy. Develop the technology of direct anaerobic dehydrogenation of methane to chemical products, replace the petroleum route or an important supplement with...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/48C07C2/76C07C11/04C07C15/04
CPCY02P20/52
Inventor 金中豪宋晗刘畅宣东刘苏王仰东
Owner CHINA PETROLEUM & CHEM CORP