Magnetic iron-based composite oxide catalyst and preparation method thereof

A technology of composite oxides and catalysts, applied in the direction of metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the limitations of large-scale industrial applications and immature preparation processes , Low temperature denitrification activity and other problems, to achieve the effect of reducing production cost, good medium and low temperature denitrification activity, and wide denitrification temperature window

Inactive Publication Date: 2016-05-25
UNIV OF SHANGHAI FOR SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

And studies have shown that: magnetic γ-Fe 2 o 3 The denitrification performance is better than that of non-magnetic α-Fe 2 o 3 ; but the magnetic γ-Fe 2 o 3 The medium and low temperature denitrification activity is low, and the preparation process is not mature enough, which limits its large-scale industrial application; if the denitrification temperature window can be extended to the medium and low temperature region, and the medium and low temperature SCR denitrification activity can be improved at the same time

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Step 1, dissolving ferrous sulfate and titanium sulfate in water to obtain a mixed solution, controlling the molar ratio of Fe:Ti to be 1:1, firstly continuing magnetic stirring for 1 hour at room temperature for mixing.

[0019] Step 2, then slowly drop the mixed solution into excess ammonia water for co-precipitation, the co-precipitation process is carried out under the mechanical seal and air isolation, until the pH value of the mixed solution precipitation is 9 to 10, the precipitation is complete, filtered and washed to obtain filter cake.

[0020] Step 3: Put the filter cake in a microwave test bench and microwave at 210W for 40 minutes, put the microwave-treated sample into a muffle furnace, and calcinate and activate it in air at 500°C for 5 hours to prepare a magnetic iron-based composite oxide catalyst.

[0021] Grinding and sieving the prepared magnetic iron-based composite oxide catalyst, and taking 40-60 meshes for use as magnetic iron-based composite oxid...

Embodiment 2

[0023] Step 1, dissolving ferrous sulfate and titanium sulfate in water to obtain a mixed solution, controlling the molar ratio of Fe:Ti to be 3:1, and firstly continuing magnetic stirring for 1 hour at room temperature for mixing.

[0024] Step 2, then slowly drop the mixed solution into excess ammonia water for co-precipitation, the co-precipitation process is carried out under the mechanical seal and air isolation, until the pH value of the mixed solution precipitation is 9 to 10, the precipitation is complete, filtered and washed to obtain filter cake.

[0025] Step 3: Put the filter cake in a microwave test bench and microwave at 210W for 40 minutes, put the microwave-treated sample into a muffle furnace, and calcinate and activate it in air at 500°C for 5 hours to prepare a magnetic iron-based composite oxide catalyst.

[0026] The prepared magnetic iron-based composite oxide catalyst was ground and sieved, and 40-60 meshes were taken for use as catalyst B. According to...

Embodiment 3

[0028] Step 1, dissolving ferrous sulfate and titanium sulfate in water to obtain a mixed solution, controlling the molar ratio of Fe:Ti to 1:0.1, and firstly continuing magnetic stirring for 1 hour at room temperature for mixing.

[0029] Step 2, then slowly drop the mixed solution into excess ammonia water for co-precipitation, the co-precipitation process is carried out under the mechanical seal and air isolation, until the pH value of the mixed solution precipitation is 9 to 10, the precipitation is complete, filtered and washed to obtain filter cake.

[0030] Step 3: Put the filter cake in a microwave test bench and microwave at 210W for 40 minutes, put the microwave-treated sample into a muffle furnace, and calcinate and activate it in air at 500°C for 5 hours to prepare a magnetic iron-based composite oxide catalyst.

[0031] Grinding and sieving the prepared magnetic iron-based composite oxide catalyst, and taking 40-60 meshes for use as magnetic iron-based composite oxi...

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Abstract

The invention provides a preparation method of a magnetic iron-based composite oxide catalyst. According to the preparation method, soluble ferrous salt and soluble titanium salt are prepared into a water solution according to the molar ratio of the iron element to the titanium element of 1:0.1-10, the water solution is stirred magnetically at normal temperature for 0.5-3 hours, and then a mixed solution is obtained; the mixed solution is stirred mechanically at normal temperature under a mechanically sealed condition or the condition that nitrogen is led into to remove oxygen, excessive alkaline precipitators are added dropwise at the same time till the pH is equal to 9-10, and after the mixed solution is completely precipitated, the precipitate is filtered and washed to obtain a filter cake; the filter cake is dried, then the processed filter cake is put in a muffle furnace for calcined activation for 3-6 hours at the temperature of 300-600 DEG C, and the magnetic iron-based composite oxide catalyst is prepared. According to the magnetic iron-based composite oxide catalyst, non-toxic components are adopted, and harm to human health and the ecological environment will not be caused; under the condition of a high air speed ratio, the catalyst has good medium and low temperature denitration cavity and can be used for removing nitric oxide in exhaust fume at a fire coal fixing source.

Description

technical field [0001] The invention belongs to the technical field of catalysts and their preparation, and in particular relates to a magnetic iron-based composite oxide catalyst and a preparation method thereof. Background technique [0002] The flue gas emitted by coal-fired stationary sources such as thermal power plants contains a large amount of nitrogen oxides, sulfur oxides, and carbon dioxide, among which nitrogen oxides (NO x , mainly NO and NO 2 ) will cause major environmental problems such as acid rain, photochemical smog, ozone depletion and greenhouse effect, and cause great harm to the ecological environment and human health. [0003] At present, for the NO in the tail flue gas of coal-fired stationary sources such as thermal power plants x Purification technologies mainly include: low NO x Combustion technology, reburning and advanced reburning technology, selective non-catalytic reduction technology (SNCR) and selective catalytic reduction technology (NH...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/745B01D53/86B01D53/56
CPCB01J23/745B01D53/8628
Inventor 熊志波武超周飞金晶林郁郁刘敦禹王秋麟王银鑫张志彪汪峻凯周文凯丛博睿
Owner UNIV OF SHANGHAI FOR SCI & TECH
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