A kind of modified ZSM-5 molecular sieve catalyst and preparation method thereof

A technology of ZSM-5 and molecular sieve, which is applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of increased production costs, high unit energy consumption of products, catalyst deactivation, etc., and achieve enhanced adsorption Effects of dissociation ability, decrease in carbon deposition rate, and decrease in reaction temperature

Active Publication Date: 2018-01-30
GUIZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the higher reaction temperature in industrialization not only increases the unit energy consumption of the product, but also accelerates the formation of carbon deposits, resulting in rapid deactivation of the catalyst and the need for frequent regeneration, further increasing the production cost of the product
It can be seen that the existing MTO process has shortcomings such as high reaction temperature, high energy consumption per unit of product, easy carbon deposition and deactivation of the catalyst, and frequent regeneration.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] A preparation method of a modified ZSM-5 molecular sieve catalyst, comprising the following steps:

[0016] (1) Modification and preparation of Ag / ZSM-5 molecular sieve: using the equal volume impregnation method, the silver nitrate solution and ZSM-5 molecular sieve (silicon-aluminum ratio 100) were mixed evenly according to the silver loading of 10 wt.%, and impregnated at room temperature for 10 hours. Dry at 85°C to constant weight, bake at 550°C for 5h, and then cool to room temperature;

[0017] (2) Modification and preparation of I-Ag / ZSM-5 molecular sieve: Using the equal-volume impregnation method, the hydroiodic acid solution was mixed with the Ag / ZSM-5 molecular sieve prepared in step (1) according to the loading capacity of 10 wt.%. Ultrasonic impregnation at room temperature for 30 minutes, followed by conventional impregnation for 12 hours, and dried at 105°C until constant weight.

[0018] The modified I-Ag / ZSM-5 catalyst was used in the MTO process (at ...

Embodiment 2

[0020] A preparation method of a modified ZSM-5 molecular sieve catalyst, comprising the following steps:

[0021] (1) Modification and preparation of Ag / ZSM-5 molecular sieve: using the equal volume impregnation method, mix the silver nitrate solution and ZSM-5 molecular sieve (silicon-aluminum ratio 100) evenly according to the silver loading of 1 wt.%, and impregnate at room temperature for 10 hours. Dry at 85°C to constant weight, bake at 550°C for 5h, and then cool to room temperature;

[0022] (2) Modification and preparation of I-Ag / ZSM-5 molecular sieve: Using the equal volume impregnation method, the potassium iodide solution was mixed with the Ag / ZSM-5 molecular sieve prepared in step (1) according to the loading capacity of 1 wt.%. Ultrasonic impregnation for 10 minutes, followed by conventional impregnation for 2 hours, and dried at 50°C to constant weight.

[0023] The modified I-Ag / ZSM-5 catalyst was used in the MTO process (at normal pressure, reaction temperat...

Embodiment 3

[0025] A preparation method of a modified ZSM-5 molecular sieve catalyst, comprising the following steps:

[0026] (1) Modification and preparation of Ag / ZSM-5 molecular sieve: using the equal volume impregnation method, mix the silver nitrate solution and ZSM-5 molecular sieve (silicon-aluminum ratio 400) evenly according to the silver loading of 1 wt.%, and impregnate at room temperature for 10 hours. Dry at 85°C to constant weight, bake at 550°C for 5h, and then cool to room temperature;

[0027] (2) Modification preparation of I-Ag / ZSM-5 molecular sieve: Using the equal volume impregnation method, the iodine-methanol solution was mixed with the Ag / ZSM-5 molecular sieve prepared in step (1) according to the loading capacity of 1 wt.%. Ultrasonic impregnation at room temperature for 10 minutes, followed by conventional impregnation for 2 hours, and dried at 50°C until constant weight.

[0028] The modified I-Ag / ZSM-5 catalyst was used in the MTO process (at normal pressure,...

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PUM

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Abstract

The invention discloses a preparing method of a modified ZSM-5 molecular sieve based catalyst.The preparing method comprises the following steps that firstly, modification preparation of an Ag / ZSM-5 molecular sieve is carried out, wherein an equivalent-volume impregnation method is adopted, a silver nitrate solution and a ZSM-5 molecular sieve are mixed evenly according to the Ag loading amount of 1-10wt%, room-temperature impregnation is carried for 10 h, and the mixture is dried to the constant weight at 85 DEG C, roasted for 5 h at 550 DEG C, and then cooled to the room temperature; secondly, modification preparation of an I-Ag / ZSM-5 molecular sieve is carried out, wherein the equivalent-volume impregnation method is adopted, an iodine-containing speciation solution and the Ag / ZSM-5 molecular sieve obtained in the first step are mixed evenly according to the loading amount of 1-10wt%, room-temperature ultrasonic impregnation is carried for 10-30 min first, then conventional impregnation is carried out for 2-12 h, and the mixture is dried to the constant weight at 50-105 DEG C.By means of the preparing method of the modified ZSM-5 molecular sieve based catalyst, the low-temperature conversion rate of methyl alcohol can be increased, the low-carbon olefin selectivity can be improved, and the service life is long.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, and in particular relates to a preparation method of a modified ZSM-5 molecular sieve catalyst. Background technique [0002] ZSM-5 molecular sieve is a kind of SiO 4 and AlO 4 A zeolite microporous molecular sieve composed of tetrahedrons and having a three-dimensional cross network straight channel structure. Because of its good hydrothermal stability, large specific surface area and strong shape-selective catalytic function, it has been widely used in coal-based methanol production of low-carbon olefins (MTO) technology. [0003] Due to the large pores and strong surface acidity of ZSM-5 molecular sieve, the industrial application usually needs to modify the molecular sieve. At present, ZSM-5 molecular sieves are mainly modified by various methods such as impregnation or doping of various metal elements, acid-base or high-temperature hydrothermal desilication and dealumination. A...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/44
CPCB01J29/44B01J2229/183
Inventor 刘飞曹建新林倩王晓丹
Owner GUIZHOU UNIV
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