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Wide-temperature-window SCR (selective catalytic reduction) catalyst with modified TiO2 as carrier as well as preparation method and application of SCR catalyst

A kind of SCR catalyst and catalyst technology, which is applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of difficulty in meeting emission standards and low purification efficiency, and achieve The effect of wide active temperature range, reduced environmental hazards, and reduced production costs

Inactive Publication Date: 2018-11-13
JIANGSU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The former, NO X The purification efficiency is low, and it is difficult to meet strict emission standards. Therefore, selective catalytic reduction technology is the main engineering technology to achieve the goal of the "Air Pollution Prevention and Control Action Plan"

Method used

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  • Wide-temperature-window SCR (selective catalytic reduction) catalyst with modified TiO2 as carrier as well as preparation method and application of SCR catalyst
  • Wide-temperature-window SCR (selective catalytic reduction) catalyst with modified TiO2 as carrier as well as preparation method and application of SCR catalyst
  • Wide-temperature-window SCR (selective catalytic reduction) catalyst with modified TiO2 as carrier as well as preparation method and application of SCR catalyst

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0024] Add 0.128mol acetylacetone to 0.064mol n-tetrabutyl titanate to make [Ti] / [C 5 h 8 o 2 ] was 1:2; then 50mL of ethanol solution was added, and the sol was obtained after stirring. The sol was concentrated in a water bath at 60°C for 4h, dried at 120°C for 6h, and then calcined at 500°C for 2h to obtain an undoped titanium dioxide carrier.

[0025] The prepared undoped titania carrier was immersed in an ammonium metavanadate aqueous solution, refluxed in a water bath at 60°C for 4h, dried at 120°C for 6h, and then calcined at 350°C for 4h. Among them, V 2 o 5 The loading amount is 1wt%.

[0026] Using the fixed bed activity test device, at a space velocity of 27314h -1 Under conditions, NO concentration 500ppm, NH 3 / NO=1 and O 2 is 5%, evaluate the catalyst that embodiment one obtains to the influence of NO removal rate, the result is as follows figure 1 As shown, the denitrification rate is 89.63% at 330°C.

example 2

[0028] Add 0.128mol acetylacetone to 0.064mol n-tetrabutyl titanate to make [Ti] / [C 5 h 8 o 2 ] at a ratio of 1:2; then add stoichiometric urea and thiourea, and then add 50 mL of ethanol solution, after stirring to obtain a sol, concentrate the sol in a water bath at 60°C for 4 hours, dry it at 120°C for 6 hours, and then dry it at 500°C Calcined at lower temperature for 2 hours to obtain S, N co-doped titania carrier, wherein the added amount of urea is [N] / [Ti]=0.01 in molar ratio, and the added amount of thiourea is [S] / [Ti]=0.03 in molar ratio.

[0029] The prepared doped catalyst was immersed in ammonium metavanadate aqueous solution, refluxed in a water bath at 60°C for 4h, dried at 120°C for 6h, and then calcined at 350°C for 4h. Among them, V 2 o 5 The loading amount is 1wt%.

[0030] Using the fixed bed activity test device, at a space velocity of 27314h -1 Under conditions, NO concentration 500ppm, NH 3 / NO=1 and O 2 It is 5%, evaluates the influence that th...

example 3

[0032] Add 0.128mol acetylacetone to 0.064mol n-tetrabutyl titanate to make [Ti] / [C 5 h 8 o 2 ] at a ratio of 1:2; then add stoichiometric urea and thiourea, and then add 50 mL of ethanol solution, after stirring to obtain a sol, concentrate the sol in a water bath at 60°C for 4 hours, dry it at 120°C for 6 hours, and then dry it at 500°C Calcined for 2 hours to obtain S, N co-doped titanium dioxide carrier, wherein the added amount of urea is based on molar ratio [N] / [Ti]=0.03, and the added amount of thiourea is based on molar ratio [S] / [Ti]=0.03 .

[0033] The prepared doped catalyst was immersed in ammonium metavanadate aqueous solution, refluxed in a water bath at 60°C for 4h, dried at 120°C for 6h, and then calcined at 350°C for 4h. Among them, V 2 o 5 The loading amount is 1wt%.

[0034] Using the fixed bed activity test device, at a space velocity of 27314h -1 Under conditions, NO concentration 500ppm, NH 3 / NO=1 and O 2is 5%, evaluate the catalyst that embodi...

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Abstract

The invention belongs to the technical field of environmental protection and relates to a wide-temperature-window SCR (selective catalytic reduction) catalyst with modified TiO2 as a carrier as well as a preparation method and an application of the SCR catalyst, in particular to a catalyst which utilizes S-N co-doped TiO2 as the carrier and used for flue gas denitrification based on wide active temperature window, a preparation method of the catalyst and an application of the catalyst in denitration treatment of exhaust gas containing nitric oxide. The catalyst comprises a catalyst carrier anda catalyst active component. The preparation method of the catalyst comprises steps as follows: (1), the S-N co-doped modified TiO2 carrier is prepared with a sol-gel method; (2), the active component is supported on the carrier with an impregnation method, and the wide-temperature-window SCR denitration catalyst can be obtained. The TiO2 carrier is subjected to non-metal element doped modification and the preparation conditions are optimized, so that the denitration efficiency of the catalyst is improved, and the catalytic activity temperature window is broadened.

Description

technical field [0001] The invention relates to an SCR catalyst, a preparation method and an application thereof, in particular to the application of the SCR catalyst with low vanadium, high catalytic efficiency and low activation temperature to catalyze denitrification in fixed source flue gas. Background technique [0002] Currently, NO X become following SO 2 Pollutants that are subject to total amount control later. The total amount control and reduction is mainly aimed at denitrification of flue gas from power plants, flue gas denitrification of coal-fired boilers, and treatment of motor vehicle exhaust. The strict control of nitrogen oxides indicates that my country has moved from simply controlling acid rain to SO 2 A new step has been taken in the direction of comprehensive control of acid gas emissions. [0003] Currently, in industry, NO X The mainstream technologies for emission control include selective non-catalytic reduction (SNCR) and selective catalytic ...

Claims

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Application Information

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IPC IPC(8): B01J27/24B01D53/86B01D53/56
CPCB01D53/8628B01D2258/0283B01J23/002B01J27/24
Inventor 赵炜张凯王爱健窦生平吴里程王谦
Owner JIANGSU UNIV