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Method for preparing alumina-supported perovskite-type oxide composition, alumina-supported perovskite-type oxide composition and use thereof

An alumina-supported, perovskite-type technology, used in metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, separation methods, etc.

Pending Publication Date: 2022-07-08
SASOL GERMANY GMBH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the crystallite size is not reported, relatively sharp reflections in the X-ray diffraction pattern indicate perovskite crystallites larger than 5 nm

Method used

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  • Method for preparing alumina-supported perovskite-type oxide composition, alumina-supported perovskite-type oxide composition and use thereof
  • Method for preparing alumina-supported perovskite-type oxide composition, alumina-supported perovskite-type oxide composition and use thereof
  • Method for preparing alumina-supported perovskite-type oxide composition, alumina-supported perovskite-type oxide composition and use thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0078] Example 1 - Perovskite La with 20 wt% 0,5 Sr 0,5 Fe 0,5 Ti 0,5 O 3 of composite materials

[0079] Prepared with 10 wt % La by mixing an aqueous lanthanum acetate solution with a 5 wt % boehmite aqueous suspension 2 O 3 gamma alumina. The mixture was then spray dried and calcined at 500°C for 1 hour.

[0080] La-doped alumina was impregnated with a mixed solution of strontium acetate, ferric ammonium citrate, and Tyzor LA (titanium solution) by incipient wetness impregnation to achieve 4.8 wt% SrO, 3.8 wt% Fe after calcination 2 O 3 and 3.8 wt% TiO 2 load amount. The products were calcined at 850°C for 3 hours and 700°C for 4 hours, respectively.

[0081] figure 1 The X-ray diffraction patterns of the material obtained by Example 1 after calcination at 850°C for 3 hours and 700°C for 4 hours are shown.

Embodiment 2

[0082] Example 2 - Perovskite La with 20 wt% 0,5 Sr 0,5 Fe 0,5 Zr 0,5 O 3 of composite materials

[0083] Prepared by mixing an aqueous lanthanum acetate solution with an aqueous suspension of 5 wt % boehmite containing 7.8 wt % La 2 O 3 gamma alumina. The mixture was then spray dried and calcined at 500°C for 1 hour.

[0084] Doped alumina was impregnated with a mixed solution of ferric ammonium citrate, zirconium acetate, and strontium acetate by incipient wetness impregnation to achieve 3.4 wt% Fe 2 O 3 , 5.3 wt% ZrO 2 and a loading of 4.4 wt% SrO. The products were calcined at 850°C for 3 hours and 700°C for 4 hours, respectively.

[0085] exist figure 2 In , the X-ray diffraction patterns of the material obtained after calcination at 850°C for 3 hours and 700°C for 4 hours are shown.

Embodiment 3

[0100] Example 3 - Perovskite LaFeO with 10 wt% 3 of composite materials

[0101] Prepared by mixing an aqueous lanthanum acetate solution with an aqueous suspension of 5 wt % boehmite containing 11.7 wt % La 2 O 3 gamma alumina. The mixture was then spray dried and calcined at 500°C for 1 hour.

[0102] Impregnation of doped alumina with a solution of ferric ammonium citrate by incipient wetness impregnation to achieve 3.3 wt% Fe 2 O 3 load amount. The products were calcined at 850°C for 3 hours and 700°C for 4 hours, respectively.

[0103] exist Figure 5 In , the X-ray diffraction pattern of the material obtained after calcination at 700°C for 4 hours is shown.

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Abstract

The present invention relates to a process for preparing an alumina-supported perovskite-type oxide composition, an alumina-supported perovskite-type oxide composition, and the use of such an alumina-supported perovskite-type oxide composition in a catalytic system for emission control applications.

Description

technical field [0001] The present invention relates to methods for preparing alumina supported perovskite oxide compositions, alumina supported perovskite oxide compositions and their use in catalytic systems for emission control applications. Background technique [0002] In order to reduce the NOx content in the exhaust gases of lean burn engines, specified NOx aftertreatment systems are required. This is because it is not possible to reduce NOx to N under normal oxidizing conditions as in a three-way catalyst operating near stoichiometric conditions 2 . Therefore, a special exhaust gas aftertreatment catalyst has been developed that contains materials capable of storing NOx (eg, in the manner of nitrates / nitrites in lean conditions). By applying less stoichiometric or enriched operating conditions, the stored NOx can be converted to nitrogen gas and the stored material can be regenerated. Such catalysts are often referred to as (lean) NOx capture catalysts. The NOx c...

Claims

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Application Information

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IPC IPC(8): B01J21/04
CPCB01J2523/00B01J21/04B01J23/002B01J37/0201B01J37/08B01D53/9422B01D2255/2092B01D2255/204B01D2255/20738B01D2255/20707B01D2255/20715B01D2255/2063B01D2255/402Y02T10/12B01J35/23B01J35/00B01J35/30B01J35/40B01J2523/24B01J2523/3706B01J2523/48B01J2523/842B01J2523/47B01D53/8628B01J6/001B01J23/83B01J35/613B01J35/615B01J35/633B01J35/635B01J35/638
Inventor T·哈梅宁M·舍尼博恩
Owner SASOL GERMANY GMBH