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Preparation and application of embedded microporous-mesoporous composite molecular sieve methanation catalyst

A molecular sieve methane, mesoporous molecular sieve technology, applied in the direction of molecular sieve catalysts, including molecular sieve catalysts, carbon compound catalysts, etc., can solve the problems of low hydrothermal stability, low-temperature catalytic activity needs to be improved, etc., to achieve excellent hydrothermal stability, Cost-effective, excellent high temperature performance

Active Publication Date: 2018-09-25
SHIJIAZHUANG VOCATIONAL TECH INST
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

Chinese invention patent application number 201210457434.5 discloses in-situ metal-doped mesoporous molecular sieves and their uses. The mesoporous molecular sieve MCM-41 is used as the carrier, and metal Ni is used as the main active component to dope into the MCM-41 framework structure, and used In the methanation reaction, compared with the supported catalyst, it shows good high temperature resistance performance, but its catalytic activity, especially the low temperature catalytic activity needs to be improved, and its hydrothermal stability is not high

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  • Preparation and application of embedded microporous-mesoporous composite molecular sieve methanation catalyst

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preparation example Construction

[0025] The preparation method of the embedded microporous-mesoporous composite molecular sieve methanation catalyst comprises the following steps:

[0026] (1) prepare Ni salt solution;

[0027] (2) Disperse the ZSM-5 microporous molecular sieve in the NaOH solution, add the template agent CTAB, stir vigorously, drop the silicon source TEOS at the same time, add the prepared Ni salt solution dropwise, stir vigorously for a certain period of time, and transfer to water Crystallization in a thermal reactor;

[0028] (3) The raw solution after crystallization is cooled to room temperature, suction-filtered, washed until neutral, vacuum-dried, and roasted to obtain a catalyst, and the Ni loading in the catalyst is 1-10 wt%.

[0029] It is worth noting that the Ni salt is nickel sulfate, nickel chloride, nickel nitrate and nickel acetate; the solvent used in the Ni salt solution is deionized water, ethanol; the hydrothermal synthesis temperature is 80 ~ 150°C, preferably 100-120°...

Embodiment 1

[0032] Embodiment 1: The preparation method of embedded microporous-mesoporous composite molecular sieve methanation catalyst, its steps are: take by weighing 1.6g nickel nitrate hexahydrate and dissolve in 20ml deionized water, configure nickel nitrate aqueous solution; 3.3g ZSM- 5 molecular sieves are dispersed in NaOH solution, the solution is heated to 40°C, a certain amount of template agent (hexadecyltrimethylammonium bromide) is added under vigorous stirring, nickel nitrate aqueous solution and silicon source (tetraethyl orthosilicate) Slowly add to the solution, the pH value of the solution is adjusted to 11, the molar ratio of each substance in the solution is: 1.0ZSM-5: 0.12Ni: 0.12CTAB: 1.0TEOS: 0.2NaOH: 100H 2 O. The mixed solution was vigorously stirred and aged for 2 hours, then moved to a hydrothermal reaction kettle, crystallized at 100°C for 72 hours, cooled rapidly to room temperature, filtered, washed until neutral, dried overnight at 100°C, and calcined at ...

Embodiment 2

[0033] Embodiment 2: The preparation method of embedded microporous-mesoporous composite molecular sieve methanation catalyst, its step is: take by weighing 3.2g nickel nitrate hexahydrate and dissolve in 20ml deionized water, configure nickel nitrate aqueous solution; 3.3g ZSM- 5 molecular sieves are dispersed in NaOH solution, the solution is heated to 40°C, a certain amount of template agent (hexadecyltrimethylammonium bromide) is added under vigorous stirring, nickel nitrate aqueous solution and silicon source (tetraethyl orthosilicate) Slowly add to the solution, the pH value of the solution is adjusted to 11, the molar ratio of each substance in the solution is: 1.0ZSM-5: 0.12Ni: 0.12CTAB: 1.0TEOS: 0.2NaOH: 100H 2 O. The mixed solution was vigorously stirred and aged for 2 hours, then moved to a hydrothermal reaction kettle, crystallized at 100°C for 72 hours, cooled rapidly to room temperature, filtered, washed until neutral, dried overnight at 100°C, and calcined at 55...

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Abstract

The invention discloses preparation and application of an embedded microporous-mesoporous composite molecular sieve methanation catalyst, and relates to the technical field of methanation catalysts. Acomposite molecular sieve ZSM-5 / MCM-41 composed of a mesoporous molecular sieve MCM-41 and a microporous molecular sieve ZSM-5 is adopted as a carrier, and Ni is adopted as an active component. The active component Ni is embedded into the skeleton structure of the microporous-mesoporous composite molecular sieve through an in-situ synthesis process. The catalyst includes 1-10 wt% of the Ni, withthe balance being the microporous-mesoporous molecular sieve ZSM-5 / MCM-41. The catalyst has microporous and mesoporous structures and high methane selectivity, and has advantages of low active component loading, high activity, good high-temperature resistance, good hydrothermal stability, long catalyst service lifetime, and the like. The catalyst has a good industrial application prospect.

Description

technical field [0001] The present invention relates to the technical field of methanation catalysts, in particular to a method for preparing a microporous-mesoporous composite molecular sieve ZSM-5 / MCM-41 methanation catalyst embedded with active components in situ and its application in the preparation of SNG . Background technique [0002] In recent years, with the implementation of my country's sustainable development strategy and environmental protection policy, the demand for clean energy is increasing. As a high-quality and efficient clean energy, natural gas is highly sought after by the international market, and the consumer market is growing rapidly. Therefore, my country's demand for natural gas is increasing, the gap between supply and demand is constantly expanding, and the degree of dependence on foreign countries is gradually increasing. As a substitute and supplement for liquefied petroleum gas and natural gas, coal-to-natural gas can optimize the structure ...

Claims

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Application Information

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IPC IPC(8): B01J29/46C07C1/04C07C9/04
CPCB01J29/005B01J29/0333B01J29/46B01J2229/183C07C1/0435C07C1/0445C07C2529/46C07C9/04
Inventor 张加赢耿海波郝卓莉
Owner SHIJIAZHUANG VOCATIONAL TECH INST