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An iron-tungsten composite oxide denitration catalyst with flake-like structure and its preparation method and application

A composite oxide and flower-shaped technology, applied in the field of catalytic denitrification, can solve the problems of poor water resistance, sulfur resistance and thermal stability, limit large-scale industrial application, high denitrification activity temperature, etc., achieve low cost, good resistance to SO2 and H2O poisoning ability, the effect of high N2 selectivity

Active Publication Date: 2016-01-20
UNIV OF JINAN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Fe-ZSM-5 (K. Krishna, et al., Catal. Today, 2006, 114:23), Fe 2 o 3 (X.L.Mou, etal., Angew.Chem.Int.Ed.2012,51:1) and Fe-Ti composite oxide (F.D.Liu, etal., Chem.Commun.,2008:2043) catalysts have shown good However, Fe-based catalysts usually have high denitrification activity temperature, poor water and sulfur resistance and thermal stability, and the preparation process is complicated, which limits their large-scale industrial application.

Method used

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  • An iron-tungsten composite oxide denitration catalyst with flake-like structure and its preparation method and application
  • An iron-tungsten composite oxide denitration catalyst with flake-like structure and its preparation method and application
  • An iron-tungsten composite oxide denitration catalyst with flake-like structure and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Weigh 1.9791gNa 2 WO 4 2H 2 O, completely dissolved in 200mL deionized water, weighed 6.6732g FeSO 4 ·7H 2 O and 100mgC 6 h 8 o 6 , completely dissolved in 100mL deionized water. Put the tungsten-containing aqueous solution into a constant temperature water bath and keep the temperature at 35 o C. Add the iron-containing aqueous solution drop by drop to the vigorously stirred solution, and keep the pH of the mixed solution in the range of 6-10 during the titration process. If the pH is lower than this range, add ammonia water to adjust. After the titration is completed, add ammonia water to adjust the mixture The pH of the solution was 8, and the stirring was continued for 3 hours. After the reaction, wash the precipitate with deionized water and ethanol several times until the filtrate is neutral, and put the filter cake in a drying box for 70 o C dried for 12 hours, and the dried sample was placed in a muffle furnace at 500 o C roasting for 5 hours to obtain...

Embodiment 2

[0052] Identical with embodiment 1 method, difference is: the sample after drying is put into muffle furnace 800 o C roasting for 5 hours to obtain iron-tungsten composite oxide. XRD results (see attached Figure 4 ) shows that the product presents a strong diffraction peak, which is Fe 2 o 3 and Fe 2 WO 6 The mixed phase of the two phases shows that after the catalyst is calcined at high temperature, the original highly dispersed iron and tungsten species aggregate to form a stable phase with high crystallinity. photo by SEM (see attached Figure 5 ) It can be seen that the unique flake-like structure of the product disappears, and it is completely composed of particles, and the particle size is less than 100nm. ICP-AES confirms that its component content is identical with embodiment 1 product.

[0053] Weigh 400 mg of the above-prepared iron-tungsten composite oxide, press it into a tablet, and sieve out 40-60 mesh particles as a catalyst for denitration performance t...

Embodiment 3

[0057] Identical with embodiment 1 method, difference is: the soluble iron salt of selection is ferric sulfate, takes by weighing Fe 2 (SO 4 ) 3 9.5971g as iron source. XRD results (see attached Figure 6 ) shows that the product has no obvious diffraction peaks, indicating that the catalyst is amorphous. photo by SEM (see attached Figure 7 ) It can be seen that the product is only composed of particles.

[0058] Weigh 400 mg of the above-prepared iron-tungsten composite oxide, press it into tablets, and sieve out 40-60 mesh particles as a catalyst for denitration performance test. The denitration rate test results are shown in Table 3.

[0059]

[0060] As can be seen from the above table: the catalyst is at 225-450 o In the C temperature range, the denitrification efficiency is significantly lower than that of the sample of Example 1, only at 250-400 o In the C range, the denitrification efficiency is greater than 90%, while the N 2 The selectivity decreased slig...

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Abstract

The invention discloses an iron-tungsten composite oxide, which comprises three elements of iron, tungsten and oxygen. Fe and W are highly dispersed in the composite oxide, and the molar ratio of Fe and W is 5.8-12.9:1, preferably 6.8:1. 1. The iron-tungsten composite oxide of the present invention has all or part of a three-dimensional flake-like morphology, and the flake-like structure is composed of multiple petals. The invention also discloses the preparation and application of the iron-tungsten composite oxide. The preparation method of the invention is simple and easy, and the precursors adopted are common metal salts such as sulfate and tungstate, and the cost is low, easy to obtain, and convenient to realize industrial production. The obtained iron-tungsten composite oxide with flake-like structure has high catalytic activity and N2 selectivity as a denitration catalyst, wide temperature range, strong resistance to sulfur dioxide and water poisoning, and can be used for stationary source flue gas, diesel vehicle exhaust and lean combustion Purification or elimination of nitrogen oxides in gasoline engine exhaust.

Description

technical field [0001] The invention relates to an iron-tungsten composite oxide, in particular to an iron-tungsten composite oxide with a special flake-like structure, a preparation method of the composite oxide and the use of the composite oxide as a fixed source flue gas, diesel vehicle Nitrogen oxides NH in exhaust gas and lean-burn gasoline engine exhaust 3 The application of the SCR catalyst belongs to the technical field of catalytic denitrification. Background technique [0002] Nitrogen oxides (NO x ) is the main pollutant that causes acid rain and photochemical smog, and its emissions mainly come from stationary sources such as coal-fired boilers, industrial furnaces and mobile sources such as motor vehicle exhaust. My country is getting on SO 2 After the phased results of the control, during the "Twelfth Five-Year Plan" period, the NO x The total amount of emission has been controlled, that is, the NO in 2015 x The total emissions decreased by 10% compared wi...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888B01J35/02B01D53/94B01D53/90B01D53/56B01J35/00
CPCY02T10/12
Inventor 张昭良刘莹周钰浩辛颖李倩
Owner UNIV OF JINAN