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One for decomposing n 2 Efficient catalyst for o and its preparation method and application

A catalyst and high-efficiency technology, applied in physical/chemical process catalysts, separation methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of limited development and high catalyst cost, and achieve recovery of catalytic activity and high activity. , the effect of good catalytic activity

Active Publication Date: 2018-01-26
CHINA TIANCHEN ENG +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] So far, there is no mature technology for reducing exhaust emissions from adipic acid production plants in China, mainly because most of the catalysts are difficult to operate in various gases (NOx, H 2 O, SO 2 etc.) show good catalytic activity and stability under the condition of existence, and the cost of catalyst is higher, N 2 The catalytic decomposition of O requires a high temperature of about 500-800 °C, which severely limits the development of tail gas emission reduction technology for adipic acid plants.

Method used

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  • One for decomposing n  <sub>2</sub> Efficient catalyst for o and its preparation method and application
  • One for decomposing n  <sub>2</sub> Efficient catalyst for o and its preparation method and application
  • One for decomposing n  <sub>2</sub> Efficient catalyst for o and its preparation method and application

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Experimental program
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Effect test

Embodiment 1

[0039] Preparation of immobilized CoO / MgAl 2 o 4 / Al 2 o 3 catalyst:

[0040] A. will Co(NO 3 ) 2 , Mg(NO 3 ) 2 , Al(NO 3 ) 3 Dissolve in deionized water at a molar ratio of 2:1:1 to obtain a solution with a total concentration of 0.3M, and mix urea with NO in the solution 3 - The molar ratio of 4:1 was added to the solution and dissolved until the solution became transparent.

[0041] B. Adding γ-Al 2 o 3 The carrier is activated and washed with a NaOH solution with a mass concentration of 3%, immersed in the solution obtained in step A, sealed in a hydrothermal reaction kettle, taken out after in-situ growth at 90°C for 48h, filtered and washed with water, and dried at 100°C for 24h. A catalyst precursor is obtained.

[0042] C. Put the catalyst precursor prepared in step B into a muffle furnace, heat and roast from room temperature at a heating rate of 10°C / min, heat up to 700°C for 3 hours, and take out the roasted product after cooling to room temperature wi...

Embodiment 2

[0045] Preparation of immobilized MgO / ZnAl 2 o 4 / Al 2 o 3 catalyst:

[0046] (1) Zn(NO 3 ) 2 , Mg(NO 3 ) 2 , Al(NO 3 ) 3 Dissolve in deionized water at a molar ratio of 3:1:1 to obtain a solution with a total concentration of 0.2M, and mix hexamethylenetetramine with NO in the solution 3 - The molar ratio of 3:1 was added to the solution and dissolved until the solution became transparent.

[0047] (2) Add γ-Al 2 o 3 Carrier with a mass concentration of 5% (NH 4 ) 2 SO 4 The solution was activated and washed, immersed in the solution obtained in step A, sealed in a hydrothermal reaction vessel, taken out after in-situ growth at 90°C for 72h, filtered and washed with water, and dried at 100°C for 12h to obtain a catalyst precursor.

[0048] (3) Put the catalyst precursor prepared in step B into a muffle furnace, heat and roast from room temperature at a heating rate of 5°C / min, heat up to 600°C for 5h, and take out the roasted product after cooling to room temp...

Embodiment 3

[0051] Preparation of solid-supported CuO / ZnAl 2 o 4 / Al 2 o 3 catalyst:

[0052] (1) Adding Cu(NO 3 ) 2 , Zn(NO 3 ) 2 , Al(NO 3 ) 3 Dissolve in deionized water at a molar ratio of 0.5:0.5:1 to obtain a solution with a total concentration of 0.1M. Combine urea with NO 3 The molar ratio of 5:1 was added to the solution and dissolved until the solution became transparent.

[0053] (2) Activate and wash the gamma-Al2O3 carrier with a 1% NaOH solution, immerse it in the solution obtained in step A, seal it in a hydrothermal reaction kettle, take it out after growing in situ at 120°C for 60h, filter and wash it with water, and Dry at 90° C. for 10 h to obtain a catalyst precursor.

[0054] (3) Put the catalyst precursor prepared in step B into a muffle furnace, heat and roast from room temperature at a heating rate of 10°C / min, heat up to 500°C for 2 hours, and take out the roasted product after cooling to room temperature with the furnace to obtain Immobilized CuO / ZnA...

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Abstract

The present invention provides an efficient catalyst for decomposition of N2O and a preparation method and application thereof. The catalyst comprises an active center and a carrier; the active center includes quantum dot oxide and spinel-type structural compound, and the carrier is a Al2O3 carrier; and the catalyst has a molecular formula L IIxO / M II1-xNIII2O4 / Al2O3, wherein: L II and M II are divalent metal cations, N III is a trivalent metal cation, and x equals to 0.01-1.0. The efficient catalyst for decomposition of N2O has high activity, good stability and low N2O decomposition temperature, is conducive to the purification of industrial waste gas from adipic acid plant; and the catalyst for decomposing N2O can significantly reduce the N2O concentration in industrial emission, reduce air pollution and protect the environment.

Description

technical field [0001] The invention belongs to the field of catalysts used in air pollution control technology, in particular to a catalyst for decomposing N 2 High-efficiency catalysts for O and their preparation methods and applications. Background technique [0002] Domestic production of adipic acid mainly adopts cyclohexanol nitric acid oxidation method. Cyclohexanol is oxidized by nitric acid to produce adipic acid. This method has mature technology, and the product yield and purity are relatively high, but the amount of nitric acid is large, and a large amount of N 2 O, and the tail gas discharged during the production process is concentrated, large in quantity and high in purity. At present, the annual output of adipic acid is 150,000 tons by cyclohexanol nitric acid oxidation method, N 2 The annual emission of O can reach 45,000 tons. [0003] N 2 O is a kind of greenhouse gas, which has a more damaging effect on the ozone layer than chlorofluorocarbons, and i...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/75B01J23/06B01J23/80B01J23/89B01D53/86B01D53/56
CPCY02C20/10Y02P20/30
Inventor 陈涛艾晓欣刘文李亚楠江屿杨琦武陈晨徐航
Owner CHINA TIANCHEN ENG