Method for improving catalytic property of methane aromatization catalyst

A technology for catalytic performance and catalyst, which is applied in the field of molecular sieve assembly catalyst, improves catalytic performance of methane aromatization reaction catalyst, and can solve the problems of limited, unsatisfactory, low conversion rate and the like of industrialized development of oxygen-free aromatization of methane, Achieve the effect of improving anti-coking ability, long catalyst life and good catalytic performance

Inactive Publication Date: 2010-01-06
DALIAN UNIV OF TECH
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

[0004] However, since the oxygen-free aromatization of methane needs to be carried out at a temperature above 700°C, the low conversion rate and serious carbon deposition problems lead to catalyst deactivation, which greatly restricts the industrial development of the oxygen-free aromatization of methane.
Therefore, the majority of researchers have conducted a lot of research on how to improve the stability of the catalyst and how to reduce carbon deposition, such as by adding various types of metal additives, changing the type of molecular sieve carrier or performing special post-treatment on molecular sieves. Add a small amount of CO, CO to the gas 2 、H 2 O impurities and other methods to improve the activity and stability of the aromatization reaction of the catalyst, and achieved certain results, but still not satisfactory enough
In addition, so far, there has been no related report on improving the catalytic performance of methane anaerobic aromatization catalysts by directly preparing molecular sieves with hierarchical pore structures and applying them to methane anaerobic aromatization reactions

Method used

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  • Method for improving catalytic property of methane aromatization catalyst
  • Method for improving catalytic property of methane aromatization catalyst
  • Method for improving catalytic property of methane aromatization catalyst

Examples

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Effect test

Embodiment 1

[0032] Preparation of MCM-22 hierarchical structure molecular sieve assembly: 0.25g NaOH, 1.6gNaAlO 2 Soluble in 95g H 2 Mix in O to form a solution evenly, then weigh 10.7g of hexamethyleneimine and add it to the solution and stir evenly. Finally, add 31.6g of silica sol within 1 hour and keep vigorously stirring overnight to obtain a system with a molar ratio of: SiO2 : Al 2 o 3 :Na 2 O:R:H 2 O=1:0.03:0.06:2:30, followed by static aging for 24 hours. The resulting mixture was transferred to a stainless steel reaction kettle with a polytetrafluoroethylene liner at 150°C for 7 days, and the product was quenched to room temperature, washed, dried, and calcined in a muffle furnace at 550°C for 8 hours. The organic template is removed to obtain the MCM-22 zeolite molecular sieve assembly with a hierarchical pore structure. The obtained product was characterized by X-ray diffraction, scanning electron microscope, nitrogen adsorption, etc., which proved that the product is dif...

Embodiment 2

[0034] Preparation of ZSM-5 hierarchical molecular sieve assembly: 32.6g TPAOH was dissolved in 30gH at room temperature 2 Mix in O to form a solution evenly, then weigh 41.6g TEOS and slowly add the above solution dropwise, stir evenly to form solution A; another 32.6g TPAOH is dissolved in 30g H 2 Mix well in O to form a solution, then weigh 1.36g of AIP and slowly add the above solution dropwise, stir well to form solution B; after stirring for 24 hours, solutions A and B were mixed and stirred for 4 hours, and statically aged for 3 hours. The molar ratio of the obtained system is: SiO 2 : Al 2 o 3 :R:H 2 O=1:0.017:0.37:30. Then the resulting mixture was transferred to a stainless steel reaction kettle lined with polytetrafluoroethylene, and was statically crystallized at 100°C for 1 day, and then statically crystallized at 175°C for 1 day. After crystallization, it was quenched to room temperature and washed to obtain a complete Crystalline product. After drying, cal...

Embodiment 3

[0036] Preparation of Mo / HMCM-22 molecular sieve assembly catalyst with hierarchical pore structure: the Na-type MCM-22 molecular sieve assembly was exchanged 3 times with 1M ammonium nitrate solution at 80-100°C, washed 3 times with water, and then heated at 550°C Calcined in air atmosphere for 6 hours to obtain HMCM-22 for future use. Weigh 3 grams of HMCM-22, place it in 30 ml of 0.011 g / ml ammonium molybdate solution, stir and impregnate overnight. Dry at 100°C for 6 hours, and then bake in an air atmosphere at 500°C for 6 hours to obtain the product Mo / HMCM-22 assembly catalyst, which is crushed to 40 mesh and ready for use.

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Abstract

The invention relates to a method for improving the catalytic property of methane aromatization catalyst, belonging to the technical field of molecular sieve catalysis. The invention is characterized in that on the condition of no-second template, the crystal growth of zeolite molecular sieve is controlled by reasonablely controlling zeolite molecular sieve synthesis conditions such as synthesis formulation, charging sequence, ageing time, crystallization temperature, crystallization time and the like, small molecular sieve crystal is used for assembly and intergrowth to form MCM-22 and ZSM-5 molecular sieve assembly with multi-stage pore path structure, Mo or Re used can be adopted as active component to perform loading and modification to the prepared molecular sieve assembly, and the invention provides Mo-based MCM-22 and ZSM-5 molecular sieve assembly catalysts and an application thereof in methane non-oxidative aromatization reaction. The effects and the benefits of the invention is that the operation is simple, the cost is low and in methane non-oxidative aromatization reaction, the multi level structure assembly catalyst prepared by the method of the invention has better catalytic performance compared with the traditional catalyst.

Description

technical field [0001] The invention belongs to the technical field of molecular sieve catalysis, and relates to a method for improving the catalytic performance of a methane aromatization reaction catalyst, in particular to improving catalytic performance by directly preparing a molecular sieve assembly catalyst with a multi-level pore structure without a second template. performance method. Background technique [0002] Methane is the main component of natural gas and coalbed methane. The latest proven reserves show that the total reserves of methane in the world are very rich, even greater than the sum of oil and coal. As a hydrocarbon species similar to coal and petroleum, natural gas with methane as the main component will become one of the important energy sources in this century. How to use high-tech and efficient use of natural gas is a major strategic measure to alleviate the contradiction between oil supply and demand, solve the oil crisis, and ensure my country's...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/78B01J29/48B01J35/10C07C2/00C07C2/76
Inventor 王金渠杨建华初乃波于素霞鲁金明殷德宏张艳
Owner DALIAN UNIV OF TECH
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