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Platinum/cerium aluminum-molecular sieve catalyst for catalytic oxidation of ammonia gas and preparation method thereof

A catalytic oxidation and molecular sieve technology, applied in molecular sieve catalysts, physical/chemical process catalysts, separation methods, etc., to achieve the effects of easy control, high selectivity, and wide low-temperature active window

Active Publication Date: 2015-09-09
SINOCAT ENVIRONMENTAL TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] CN 103476495A discloses an ammonia oxidation catalyst and an exhaust gas purification device using it and its use method. It adopts double-layer coating, the lower layer is an inorganic material loaded with precious metals, and the upper layer is a molecular sieve catalyst. 3 It has higher catalytic oxidation activity, but also produces a higher concentration of N 2 O and NO x

Method used

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  • Platinum/cerium aluminum-molecular sieve catalyst for catalytic oxidation of ammonia gas and preparation method thereof
  • Platinum/cerium aluminum-molecular sieve catalyst for catalytic oxidation of ammonia gas and preparation method thereof
  • Platinum/cerium aluminum-molecular sieve catalyst for catalytic oxidation of ammonia gas and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0048] (1) Preparation of cerium-aluminum composite oxide

[0049] Take 261.0ml of 0.4g / ml aluminum nitrate solution, 236.7ml of 0.2g / ml cerium nitrate solution, and 758.7ml of 0.2g / ml citric acid solution and mix evenly; stir for 2h, then use a rotary evaporator to evaporate the water to dryness, 120 Dry at ℃ for 20h, and finally put it into a muffle furnace, raise the temperature from room temperature to 650℃, and bake at 650℃ for 3h to obtain a cerium-aluminum composite oxide, in which aluminum oxide and ceria The mass ratio is 1:1.

[0050] (2) Preparation of neodymium modified molecular sieve

[0051] Take 29.5ml of 0.2g / ml neodymium nitrate solution, add it to 47g ZSM-5 molecular sieve powder, put it in an oven, and dry it at 100°C for 10h; Modified molecular sieve; the neodymium element exists in the form of neodymium oxide in the neodymium modified molecular sieve, and the mass ratio of neodymium oxide to ZSM-5 molecular sieve is 6:94.

[0052] (3) Preparation of ca...

Embodiment 2

[0060] (1) Preparation of cerium-aluminum composite oxide

[0061] Take 835.3ml of 0.2g / ml aluminum nitrate solution, 252.2ml of 0.3g / ml cerium nitrate solution, and 1213.6ml of 0.2g / ml citric acid solution and mix evenly; stir for 2h, then use a rotary evaporator to evaporate the water to dryness, 120 Dry at ℃ for 20h, and finally put it into a muffle furnace, raise the temperature from room temperature to 650℃, and bake at 650℃ for 3h to obtain a cerium-aluminum composite oxide, in which aluminum oxide and ceria The mass ratio is 4:3.

[0062] (2) Preparation of neodymium modified molecular sieve

[0063] Take 23.6ml of 0.1g / ml neodymium nitrate solution, add it to 28.8g ZSM-5 molecular sieve powder, put it into an oven, and dry it at 120°C for 8h; then put it into a muffle furnace, and bake it at 650°C for 3h to get Neodymium modified molecular sieve; the neodymium element in the neodymium modified molecular sieve exists in the form of neodymium oxide, and the mass ratio ...

Embodiment 3

[0072] (1) Preparation of cerium-aluminum composite oxide

[0073] Take 348.0ml of 0.3g / ml aluminum nitrate solution, 71.1ml of 0.4g / ml cerium nitrate solution, and 664.2ml of 0.2g / ml citric acid solution and mix evenly; stir for 1.5h, and then use a rotary evaporator to evaporate the water to dryness. Dry at 100°C for 24 hours, and finally put it into a muffle furnace, raise the temperature from room temperature to 550°C, and bake at 550°C for 4 hours to obtain a cerium-aluminum composite oxide. The cerium-aluminum composite oxide contains aluminum oxide and cerium oxide The mass ratio is 5:3.

[0074] (2) Preparation of neodymium modified molecular sieve

[0075] Take 11.8ml of 0.2g / ml neodymium nitrate solution, add it to 58.8g ZSM-5 molecular sieve powder, put it into an oven, and dry it at 120°C for 8h; then put it into a muffle furnace, and bake it at 550°C for 4h to get Neodymium modified molecular sieve; the neodymium element in the neodymium modified molecular sieve...

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Abstract

The invention provides a platinum / cerium aluminum-molecular sieve catalyst for catalytic oxidation of an ammonia gas. Cordierite ceramic is utilized as a carrier for the platinum / cerium aluminum-molecular sieve catalyst, the surface of the carrier is coated with a catalyst layer, and the catalytic active site of the catalyst layer consists of a noble metal platinum, a cerium-aluminum composite oxide and a neodymium-modified molecular sieve; the mass ratio of the cerium-aluminum composite oxide to the neodymium-modified molecular sieve to the noble metal platinum is (20-80):(20-80):(0.01-0.1), and the mass ratio of cerium oxide and aluminum oxide in the cerium-aluminum composite oxide is (1-3):(1-5); the mass ratio of neodymium oxide and a molecular sieve in the neodymium-modified molecular sieve is (1-10):(90-100). The platinum / cerium aluminum-molecular sieve catalyst is also capable of achieving wide low-temperature activity window, good catalytic activity and high selectivity even at a high space velocity (SV), and is capable of effectively restraining generation of secondary pollutants of N2O, NO and NO2. The invention further provides a preparation method of the platinum / cerium aluminum-molecular sieve catalyst.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and relates to a catalyst for catalytic oxidation of ammonia and a preparation method thereof, in particular to a platinum / cerium aluminum-molecular sieve catalyst for catalytic oxidation of ammonia and a preparation method thereof. Background technique [0002] Diesel engines are being used more and more widely due to their low fuel consumption and high power. However, the high temperature and high pressure in the cylinder of diesel engines will produce a large amount of nitrogen oxides, which has brought serious environmental problems. At present, my country basically adopts Selective Catalytic Reduction (SCR) to treat nitrogen oxides produced by diesel engines, and the most widely used reducing agent is urea aqueous solution, which is hydrolyzed to generate ammonia. In order to meet stricter NOx emission standards, the following two methods are mainly adopted in the world: (1) injecting more...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/44B01D53/86B01D53/58
CPCY02C20/10
Inventor 廖传文刘小庆彭鹏孙浩李云
Owner SINOCAT ENVIRONMENTAL TECH
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