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Method for reducing nitrogen oxide in double bed combined catalyst system under enriched oxygen condition

A technology combining catalysts and nitrogen oxides, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve problems such as poor selectivity, narrow active temperature range, and poor hydrothermal stability.

Inactive Publication Date: 2005-03-30
TSINGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Molecular sieve catalysts have good activity and selectivity, but poor hydrothermal stability; noble metal catalysts have good low-temperature activity but poor selectivity; metal oxide catalysts have good high-temperature activity and thermal stability, but poor low-temperature activity
(See review literature Burch etc., Applied Catalysis B:Environ.2002,39:283-303, Keichi Shimizu etc., Catalysis Surveys from Japan, 2000,4:115-123.) So far, single catalytic component and single type It is difficult for the catalyst to operate at the actual lean exhaust temperature (about 200-500°C) and H 2 O and SO 2 Effectively purify NO in the presence of
There are many domestic researches on automobile exhaust, but most of them are about three-way catalytic converters. There are few works on selective reduction of NO under oxygen-enriched atmosphere, and they mainly focus on catalysts with a single active component.
Foreign articles and patents on the selective reduction of NO in an oxygen-rich atmosphere, such as EP0108980, US6251820, etc., such catalysts generally have a narrow activity temperature range, and some catalysts have relatively poor resistance to water and sulfur dioxide

Method used

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  • Method for reducing nitrogen oxide in double bed combined catalyst system under enriched oxygen condition
  • Method for reducing nitrogen oxide in double bed combined catalyst system under enriched oxygen condition
  • Method for reducing nitrogen oxide in double bed combined catalyst system under enriched oxygen condition

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] ①Pt / Al 2 o 3 Catalyst preparation:

[0021] 1) First prepare the H containing precious metal Pt of 4.45g / L 2 PtCl 6 weak;

[0022] 2) Take 40g of aluminum isopropoxide (AIP) and grind it into powder in a mortar; in a 1000mL rotary evaporating flask, heat 300mL of deionized water to 80°C, then add aluminum isopropoxide, and heat and stir for 1 hour;

[0023] 3) Take 65% concentrated HNO 3 3mL was added to 20mLH 2 O, stir well, put HNO 3 Add the solution dropwise to the mixed solution, and continue heating and stirring in the rotary evaporator for 1 hour to form a transparent boehmite sol;

[0024] 4) Add 22.5mL of noble metal Pt containing 4.45g / L H 2 PtCl 6 Ethanol solution, continue heating and stirring in the rotary evaporator for 1 hour;

[0025] 5) Evaporate under reduced pressure in a rotary evaporator at 85°C for 4 hours, then place it for 12 hours to age to form a gel, and dry it in an oven at 100°C for 12 hours;

[0026] 6) Sintering at 500°C for 5 ho...

Embodiment 2

[0036] ①Pt / Al 2 o 3 Catalyst preparation

[0037] 1) Take 40g of aluminum isopropoxide and grind it into powder in a mortar;

[0038] 2) Add 300mL deionized water to a 1000mL rotary evaporating flask and heat to 90°C;

[0039] 3) adding aluminum isopropoxide, heating and stirring for 3 hours;

[0040] 4) Take 65% concentrated HNO 3 3mL was added to 20mLH 2 O, stir well, put HNO 3 The solution was added dropwise to the mixed solution (dropwise), and continued to heat and stir in a rotary evaporator for 3 hours to form a transparent boehmite sol;

[0041] 5) Add 45mL of noble metal Pt containing 4.45g / L H 2 PtCl 6 Ethanol solution, continue heating and stirring in rotary evaporator for 4 hours;

[0042] 6) Use a circulating vacuum water pump to evacuate to 0.04-0.08MPa, heat and evaporate in a rotary evaporator at 90°C for 8 hours;

[0043] 7) Take out the above sol, place it for 24 hours, make it age to form a gel, and dry it in an oven at 120°C for 24 hours;

[0044...

Embodiment 3

[0053] ①Pt-Al 2 o 3 The preparation of catalyst is the same as in Example 2.

[0054] ②1% La 2 o 3 -5%SnO 2 -Al 2 o 3 Metal Oxide Catalyst Preparation

[0055] 1) Take 40g of aluminum isopropoxide and grind it into powder in a mortar;

[0056] 2) Add 300mL deionized water to a 1000mL rotary evaporating flask and heat to 90°C;

[0057] 3) adding aluminum isopropoxide, heating and stirring for 1 hour;

[0058] 4) Take 65% concentrated HNO 3 3mL was added to 20mLH 2 O, stir well, put HNO 3 The solution was added dropwise to the mixed solution (dropwise), and continued to heat and stir in a rotary evaporator for 1 hour;

[0059] 5) Prepare SnCl containing Sn50g / L 4 ·5H 2 O ethylene glycol solution and La(NO 3 ) 3 Ethylene glycol solution, respectively pipette 10.5mL of SnCl 4 ·5H 2 O ethylene glycol solution and 10 mL of La(NO 3 ) 3 Ethylene glycol solution was added dropwise, followed by heating and stirring in a rotary evaporator for 3 hours;

[0060] 6) Use...

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Abstract

The present invention relates to the NO containing waste gas purifying method in oxygen-rich atmosphere. Waste gas containing NO is first made to pass through noble metal catalyst so as to oxidize NO into NO; and hydrocarbon reducing agent is then added for a selective catalytic reduction reaction in a metal oxide catalyst system to reduce NO2 into N2, CO2 and H2O. The noble metal catalyst has the active components Pt / Al2O3; and the metal oxide catalyst system has the active components including at least one of SnO2, In2O3, Ca2O3, CoOx and NiOx. The single-component or double-component noble metal catalyst and the metal oxide catalyst are prepared through sol-gel process. The present invention can reduce NO in wide range and the NO converting rate may reach to 90%.

Description

technical field [0001] The invention relates to a method for reducing nitrogen oxides by using a double-bed combined catalyst system under oxygen-enriched conditions, that is, a method for purifying NO in exhaust gas in an oxygen-enriched atmosphere, which is suitable for lean-burn gasoline engines, diesel engines, and industrial production such as thermal power plants and smelters The NO treatment in the flue gas of oil refineries, etc. belongs to the field of environmental protection catalytic purification technology. Background technique [0002] With the advancement of science and technology, productivity has been highly developed, but the environment on which human beings depend has been greatly damaged. Serious problems such as photochemical smog, acid rain, greenhouse effect, and ozone layer hole effect, which occur frequently all over the world, are closely related to the nitrogen oxides and hydrocarbons emitted by humans into the atmosphere. NO emission sources inc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/56B01D53/86
Inventor 李俊华郝吉明傅立新朱天乐
Owner TSINGHUA UNIV