Mesoporous molecular sieve-based catalyst used for ammonia removing, and preparation method and applications thereof

A mesoporous molecular sieve and catalyst technology, applied in the chemical industry to achieve high activity

Inactive Publication Date: 2015-09-09
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At present, there is no report on the application of mesoporous

Method used

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  • Mesoporous molecular sieve-based catalyst used for ammonia removing, and preparation method and applications thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Weigh 4.0g of P123, then add 90ml of deionized water, stir for about 1 hour until completely dissolved; add 60ml, 4mol / L HCl solution to the above solution; pour it into a three-neck flask, and stir in a constant temperature water bath at 40°C for 2 hours Disperse the surfactant at a speed of 400r / min; weigh 8.5g of tetraethyl orthosilicate (TEOS), and add it dropwise to the above solution for 1 to 2 hours through a constant pressure funnel to obtain a precursor solution; continue to stir for 22 hours at a speed of 400r / min; then pour the precursor solution into the crystallization kettle, crystallize in a 100°C constant temperature drying oven for 24 hours, and separate the precipitate; then wash the precipitate to neutral; put the obtained precipitate in a 100°C constant temperature drying oven Dry it for 2-3 hours, then move it to a muffle furnace and bake it at 550°C for 6 hours (heating rate: 3°C / min) to obtain pure silicon-based mesoporous molecular sieve SBA-15. ...

Embodiment 2

[0048] Compared with Example 1, the only difference is that the loading amount of copper in this example is different, and the mass ratio of copper contained in the weighed copper nitrate to mesoporous molecular sieve is 1:25. In this example, a mesoporous molecular sieve-based catalyst with a copper loading of 4% in copper oxide was finally obtained, labeled as 4% Cu-SBA-15.

Embodiment 3

[0050] Compared with Example 1, the only difference is that the loading amount of copper in this example is different, and the mass ratio of copper contained in the weighed copper nitrate to mesoporous molecular sieve is 1:16.7. In this example, a mesoporous molecular sieve-based catalyst with a copper loading of 6% in copper oxide was finally obtained, labeled as 6% Cu-SBA-15.

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Abstract

The invention discloses a mesoporous molecular sieve-based catalyst used for ammonia removing, and a preparation method and applications thereof. The mesoporous molecular sieve-based catalyst comprises a mesoporous molecular sieve and at least one active ingredient; specific surface area of the mesoporous molecular sieve-based catalyst ranges from 400 to 750m<2>*g<-1>; the at least one active ingredient is embedded into pore passages of the mesoporous molecular sieve; particle size of the active ingredient ranges from 2 to 50nm; the active ingredient is a transition metal oxide; transition metal loading amount of the transition metal oxide accounts for 2 to 8wt% of the total weight of the mesoporous molecular sieve-based catalyst. According to the preparation method, different mesoporous molecular sieve carriers are prepared via in situ synthesis, and the mesoporous molecular sieve-based catalyst is obtained via loading of a certain amount of the active ingredient via dipping-rotary evaporation. When the mesoporous molecular sieve-based catalyst is used for an ammonia selective catalytic oxidation removing system, 100% catalytic efficiency can be achieved at 300 DEG C, energy consumption is reduced, and at the same time, catalyst catalytic efficiency and N2 selectivity are increased.

Description

technical field [0001] The invention relates to the technical field of chemical industry. More specifically, it relates to a mesoporous molecular sieve-based catalyst for ammonia removal and its preparation method and application. Background technique [0002] NH as one of air pollutants 3 It exists in many chemical productions (nitrates, nitrogenous fertilizers, petroleum refining, etc.), biological emissions, and vehicle exhaust treatment. Currently dealing with NH 3 The methods are biological, chemical and physical. Among them, due to the selective catalytic oxidation method (SCO-NH 3 ) let NH 3 with O 2 The reaction produces harmless H 2 O and N 2 , with the advantages of high reaction efficiency and short time, it is considered to be an efficient and ideal NH 3 Approach. The reaction process that it may involve is shown in the following four equations: [0003] 4NH 3 +3O 2 =2N 2 +6H 2 O (1) [0004] 4NH 3 +5O 2 =4N 2 +6H 2 O (2) [0005] 2NH 3 +2O ...

Claims

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Application Information

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IPC IPC(8): B01J29/03B01D53/86B01D53/58
CPCY02A50/20
Inventor 张润铎石兆源彭暾刘宁陈标华
Owner BEIJING UNIV OF CHEM TECH
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