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High-temperature hydrothermally stable silicon-modified SCR catalyst and preparation method thereof

An SCR catalyst, high temperature hydrothermal technology, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of reduced selectivity, inability to meet emission requirements, secondary air pollution, etc. Achieve the effect of improving hydrothermal stability, wide reaction temperature window and high hydrothermal stability

Active Publication Date: 2019-11-12
SICHUAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] V 2 o 5 -WO 3 (MO 3 ) / TiO 2 A series of catalysts (i.e. vanadium-based catalysts) have been successfully applied to stage IV (National IV) and V (National V) diesel vehicles to purify their exhaust NOx. With the more stringent sixth stage (i.e. National VI) emission standards The promulgation of this type of catalyst does not meet the National VI and higher standards for diesel vehicle exhaust NO x emission requirements
Mainly because there are still some unavoidable shortcomings of vanadium-based catalysts: the effective working window (300-400°C) of this type of catalyst cannot adapt to the temperature range of diesel vehicle exhaust (175-550°C); 3 The non-selective oxidation of NO x The purification rate drops rapidly, and a large amount of greenhouse gas N is produced 2 O, leading to the main product N 2 The selectivity of the vanadium-based catalyst is significantly reduced, and it also causes secondary pollution to the atmosphere; the thermal stability of the vanadium-based catalyst is poor, V 2 o 5 Has strong biological toxicity
However, WO 3 / CeZrO 2 After the catalyst is hydrothermally aged, Ce will be generated on the surface of the catalyst 2 (WO 4 ) 3 , leading to catalyst deactivation

Method used

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  • High-temperature hydrothermally stable silicon-modified SCR catalyst and preparation method thereof
  • High-temperature hydrothermally stable silicon-modified SCR catalyst and preparation method thereof
  • High-temperature hydrothermally stable silicon-modified SCR catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0051] (1) Weigh 8 grams of cerium-zirconium powder CeZrO 2 Add the powder into 150 ml of deionized water, add 1.4 ml of tetraethyl orthosilicate under stirring at room temperature, continue stirring for 13 hours, and continue stirring for 3 hours after standing at room temperature for 12 hours; centrifuge the obtained suspension, wash the precipitate with deionized water, and remove the precipitate Put it in a water bath at 90°C, heat and stir continuously until the water evaporates to obtain a powder; put the powder in a 120°C oven and dry for 3 hours to obtain yellow SiO 2 / CeZrO 2 -1 powder.

[0052] (2) 1.04 grams of ammonium metatungstate was dissolved in 3.05 milliliters of deionized water to obtain ammonium metatungstate solution, and 8.47 grams of SiO 2 / CeZrO 2 Add -1 powder into the ammonium metatungstate solution, stir for 30 minutes, let it stand for 10 hours, put it in a water bath at 70°C, 80°C, and 90°C for 2 hours, and then bake it at 550°C for 3 hours in a...

Embodiment 2

[0056] (1) Weigh 8 grams of cerium-zirconium powder and add it to 150 ml of deionized water, add 3.4 ml of ethyl orthosilicate under magnetic stirring at room temperature, and continue stirring for 16 hours; centrifuge the obtained salt solution, wash the precipitate, and move the precipitate to 90 ° C In a water bath, heat and stir continuously until the water evaporates to obtain a powder; put the powder in an oven at 120°C for 3 hours to obtain yellow SiO 2 / CeZrO 2 -2 powder.

[0057] (2) 1.04 grams of ammonium metatungstate was dissolved in 3.05 milliliters of deionized water to obtain ammonium metatungstate solution, and 8.47 grams of SiO 2 / CeZrO 2 -2 powder was added to the ammonium metatungstate solution, stirred for 30 minutes, and after standing for 10 hours, put it into a water bath at 70°C, 80°C, and 90°C to dry for 2 hours respectively, and then roasted at 550°C for 3 hours in an air atmosphere to obtain WO 3 / SiO 2 / CeZrO 2 Catalyst powder, where WO 3 10%...

Embodiment 3

[0061] (1) Weigh 8 grams of cerium-zirconium powder and add it to 150 ml of deionized water, add 5.4 ml of ethyl orthosilicate under magnetic stirring at room temperature, and continue stirring for 16 hours; centrifuge the obtained salt solution, wash the precipitate, and move the precipitate to 90 ° C In a water bath, heat and stir continuously until the water evaporates to obtain a powder; put the powder in an oven at 120°C for 3 hours to obtain yellow SiO 2 / CeZrO 2 -3 powder.

[0062] (2) 1.04 grams of ammonium metatungstate was dissolved in 3.05 milliliters of deionized water to obtain ammonium metatungstate solution, and 8.47 grams of SiO 2 / CeZrO 2-3 powder was added to the ammonium metatungstate solution, stirred for 30 minutes, and after standing for 10 hours, put it into a water bath at 70°C, 80°C, and 90°C for 2 hours respectively, and then roasted at 550°C for 3 hours in an air atmosphere to obtain WO 3 / SiO 2 / CeZrO 2 Catalyst powder, where WO 3 10% by weig...

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Abstract

The invention provides a silicon-modified SCR catalyst with high hydrothermal stability. The SCR catalyst is a composite oxide obtained by modifying WO<3> / Ce<x>Zr<1-x>O<2> with silicon and has a chemical formula of WO<3> / SiO<2> / Ce<x>Zr<1-x>O<2>, wherein x is more than 0 and less than 1; the mass fraction of WO<3> in the catalyst is greater than 0 and less than or equal to 15%; and the mass fraction of SiO<2> in the catalyst is in a range of 2 to 8%. The preparation method comprises the following steps: adding cerium-zirconium composite oxide powder Ce<x>Zr<1-x>O<2> into deionized water; addingethyl orthosilicate (TEOS) under stirring at room temperature, carrying out stirring for 5-15 h at first, then performing standing for 6-15 h at room temperature, continuing stirring for 1-6 h, and then carrying out solid-liquid separation to obtain a precipitate; drying the obtained precipitate to obtain SiO<2> / Ce<x>Zr<1-x>O<2> powder; and then subjecting a tungsten source to equivalent-volume impregnation into the SiO<2> / Ce<x>Zr<1-x>O<2> powder. The catalyst obtained in the invention shows excellent resistance to hydrothermal aging in the selective catalytic reduction of nitrogen oxides byammonia, has excellent catalytic activity and is friendly to environment.

Description

technical field [0001] The invention belongs to NH 3 -SCR catalyst field, specifically related to a catalytic purification of diesel vehicle exhaust NO x Gas non-vanadium based WO 3 / CeZrO 2 Composite oxide NH 3 -SCR catalyst. Background technique [0002] With the promulgation of increasingly stringent nitrogen oxide emission regulations around the world, NO in lean-burn vehicle exhaust x Purification has become one of the environmental problems that need to be solved urgently. Nitrogen oxides can cause environmental problems such as acid rain, photochemical smog, greenhouse effect and ozone hole, and cause serious harm to human health and the ecological environment. 95% NO in the atmosphere x It comes from motor vehicle exhaust (49%) and flue gas (46%) emissions from thermal power plants. Ammonia Selective Catalytic Reduction of NO x (NH 3 -SCR) is currently the most promising diesel vehicle exhaust NO x Purification technology has been industrialized in develop...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/30B01J37/03B01J37/025B01D53/94B01D53/56
CPCB01D53/9413B01D2258/012B01J23/002B01J23/30B01J37/03B01J2523/00B01J2523/3712B01J2523/41B01J2523/48B01J2523/69
Inventor 徐海迪陈耀强王健礼刘双王云林青瑾刘静莹焦毅
Owner SICHUAN UNIV
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