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Catalyst for improving methanol aromatization reaction performance, and preparation method and application thereof

A reaction performance, catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of reducing catalyst wear resistance, tedious HZSM-5, low selectivity of aromatics, etc., to achieve improved Anti-carbon performance, low price, and the effect of improving the selectivity of aromatics

Pending Publication Date: 2021-11-19
NORTHWEST UNIV(CN)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the generation of a large amount of alkanes and the dynamic process of dehydrogenation-hydrogenation in the reaction process make the problems of low selectivity and poor stability of aromatics in MTA technology restrict the industrialization of this technology.
[0004] Many researchers have studied the reaction of methanol to aromatics from two aspects of catalyst design and reaction process optimization, and have made some progress. The existing technology often supports multi-component active metals on molecular sieves, such as (Pt, Ag, etc.), but Due to the addition of these metals, the cost is also greatly increased; the process of acid-base treatment and silane modification of HZSM-5 is often too cumbersome, and multi-step modification of molecular sieves is required, which does not take advantage of the development of industrialization; for example, hollow HZSM-5, Core-shell HZSM-5 often requires the addition of expensive templates to create pores and encapsulate, which not only requires harsh synthesis conditions, but also reduces the wear resistance of the catalyst

Method used

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  • Catalyst for improving methanol aromatization reaction performance, and preparation method and application thereof
  • Catalyst for improving methanol aromatization reaction performance, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Take 0.55g of nitric acid and 1.88g of ferric nitrate in a 25ml beaker, add 2.5g of deionized water, seal and ultrasonically disperse the solution for 20min; Ferric nitrate and gallium nitrate solutions are evenly impregnated in the zeolite channels, then dried in a blast drying oven at 80°C, placed in an air atmosphere, and baked at 550°C in a muffle furnace at a heating rate of 2°C / min After 6 hours, a finished catalyst with a loading capacity of 3%Ga5%Fe / HZSM-5 was obtained.

[0037] A continuous-flow fixed-bed reactor was used to evaluate the effect of the methanol aromatization catalyst. The reactor was a U-shaped steel pipe with an inner diameter of 8 mm; the catalyst was filled, and the upper layer of the catalyst was covered with quartz wool to ensure that the bed was evenly distributed. Before the reaction, the catalyst was heated in H 2 In situ reduction at a flow rate of 25mL / min and a temperature of 500°C for 1h, then cooled to a reaction temperature of 400°...

Embodiment 2

[0041]Take 0.367g of nitric acid and 2.16g of ferric nitrate in a 25ml beaker, add 2.5g of deionized water, seal and ultrasonically disperse the solution for 30min; Ferric nitrate and gallium nitrate solutions are evenly impregnated in the zeolite channels, then dried in a blast drying oven at 80°C, placed in a nitrogen atmosphere, and baked at 500°C in a muffle furnace at a heating rate of 5°C / min After 6 hours, a finished catalyst with a loading capacity of 2%Ga-7%Fe / HZSM-5 was obtained.

[0042] A continuous-flow fixed-bed reactor was used to evaluate the effect of the methanol aromatization catalyst. The reactor was a U-shaped steel pipe with an inner diameter of 8 mm; the catalyst was filled, and the upper layer of the catalyst was covered with quartz wool to ensure that the bed was evenly distributed. Before the reaction, the catalyst was heated in H 2 In situ reduction at a flow rate of 25mL / min and a temperature of 500°C for 1h, then cooled to a reaction temperature of...

Embodiment 3

[0044] Take 0.13g of nitric acid and 0.43g of ferric nitrate in a 25ml beaker, add 2.5g of deionized water, seal and ultrasonically disperse the solution for 60min; Ferric nitrate and gallium nitrate solutions are evenly impregnated in the zeolite channels, then dried in a blast oven at 80°C, placed in an air atmosphere, and baked in a muffle furnace at a heating rate of 3°C / min to 600°C After 6 hours, a finished catalyst with a loading capacity of 1%Ga-1%Fe / HZSM-5 was obtained.

[0045] A continuous-flow fixed-bed reactor was used to evaluate the effect of the methanol aromatization catalyst. The reactor was a U-shaped steel pipe with an inner diameter of 8 mm; the catalyst was filled, and the upper layer of the catalyst was covered with quartz wool to ensure that the bed was evenly distributed. Before the reaction, the catalyst was heated in H 2 In situ reduction at a flow rate of 25mL / min and a temperature of 500°C for 1h, then cooled to a reaction temperature of 400°C, and...

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Abstract

The invention discloses a catalyst for improving methanol aromatization reaction performance, and a preparation method and application thereof. The preparation method comprises the steps: firstly, drying a carrier HZSM-5; then loading active components Ga and Fe on the dried carrier HZSM-5 by adopting an initial wet impregnation method; and roasting the obtained mixture in a nitrogen or air atmosphere to obtain the catalyst for improving the methanol aromatization reaction performance. According to the catalyst prepared by the method, CO2 which is a main gas with a greenhouse effect is effectively utilized to be converted into aromatic hydrocarbon with a high additional value in the use process, the preparation method is simple, raw materials are easy to obtain, the catalyst is green and efficient, the economic benefit is high, and the requirement of industrial production is easily met.

Description

technical field [0001] The invention belongs to the technical field of energy and chemical catalysts, and in particular relates to a catalyst for improving the performance of methanol aromatization reaction, a preparation method and an application. Background technique [0002] Aromatic hydrocarbons are an important organic reaction intermediate in the petroleum industry, and are widely used in many industries such as medicine, military industry, materials, and daily cosmetics. At present, the main source of aromatics still relies on traditional processes such as catalytic reforming in petrochemical industry. However, due to the shortage of petroleum resources, it is of great practical significance to develop a new type of aromatic hydrocarbon preparation technology. [0003] At present, in the field of coal chemical industry, coal is used as raw material to gasify CO and H 2 Synthetic methanol technology has become more and more mature, and the production of methanol is s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/46C07C15/02C07C1/20
CPCB01J29/46C07C1/20C07C15/02Y02P20/52
Inventor 马晓迅金润泽崔旭黄帆刘康儒
Owner NORTHWEST UNIV(CN)
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