Ceria-based mixed-metal oxide structure, including method of making and use

a technology of mixed metal oxide and mixed metal, applied in the direction of catalysts, physical/chemical process catalysts, bulk chemical production, etc., can solve the problems of increasing the amount of effective surface area per unit reactor volume, decreasing the effective number of sites per crystallite aggregate, etc., to increase the surface area and strengthen the structure against premature aging

Inactive Publication Date: 2003-10-02
INT FUEL CELLS
View PDF37 Cites 56 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

0030] Following drying, the oxide, or the aforedescribed formed and dried mixed metal oxide may be calcined at 250.degree. C.-600.degree. C., and preferably about 350.degree. C. -500.degree. C., for an interval sufficient to remove adsorbed species and strengthen the structure against premature aging. Lower temperatures typically mean more physisorbed and chemisorbed solvent and/or carbonates, while higher t...

Problems solved by technology

However, if that value becomes too small because of excessive pore size and/or volume, the effective number of sites pe...

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

example 4

[0050] A Ce.sub.0.625Zr.sub.0.325Pr.sub.0.05O.sub.2 catalyst support is prepared by dissolving 25.7 g of (NH.sub.4).sub.2Ce(NO.sub.3).sub.6, 6.7 g of ZrO(NO.sub.3).sub.2. xH.sub.2O, 1.63 g of Pr(NO.sub.3).sub.3 6H.sub.2O and 576 g of urea in 4800 mL of de-ionized water. The solution is heated to its boiling temperature while stirring until the coprecipitation is observed. The mixture is then aged at boiling temperature for 7 hours and then is left stirring at room temperature for 16 hours. The mixture is filtered in a Buchner funnel. The resulting filter cake is washed twice with 500 mL of de-ionized water at boiling temperature while stirring for 10 minutes, and then filtered after each washing step. Then the filter cake is washed three times with 100 mL of dried 2-propanol while in the Buchner funnel. Then, if necessary, the precipitate is mixed with 400 mL of dried 2-propanol and heated to reflux for 45 minutes and then filtered again before being extruded, as through a syringe. ...

example 5

[0052] A Ce.sub.0.625Zr.sub.0.325La.sub.0.05O.sub.2 catalyst support is prepared by dissolving 25.7 g of (NH.sub.4).sub.2Ce(NO.sub.3).sub.6, 6.7 g of ZrO(NO.sub.3).sub.2. xH.sub.2O, 1.62 g of La(NO.sub.3).sub.3 6H.sub.2O and 576 g of urea in 4800 mL of de-ionized water. The solution is heated to its boiling temperature while stirring until the coprecipitation is observed. The mixture is then aged at boiling temperature for 7 hours and then is left stirring at room temperature for 16 hours. The mixture is filtered in a Buchner funnel. The resulting filter cake is washed twice with 500 mL of de-ionized water at boiling temperature while stirring for 10 minutes, and then filtered after each washing step. Then the filter cake is washed three times with 100 mL of 2-propanol while in the Buchner funnel. Then, if necessary, the precipitate is mixed with 400 mL of dried 2-propanol and heated to reflux for 45 minutes and then filtered again before being extruded, as through a syringe. The ex...

example 6

[0054] A Ce.sub.0.80Gd.sub.0.20O.sub.2 catalyst support is prepared by dissolving 32.89 g of (NH.sub.4).sub.2Ce(NO.sub.3).sub.6, 6.77 g of Gd(NO.sub.3).sub.3 . 6H.sub.2O and 576 g of urea in 4800 mL of de-ionized water. The solution is heated to its boiling temperature while stirring until the coprecipitation is observed. The mixture is then aged at boiling temperature for 7 hours and then is left stirring at room temperature for 16 hours. The mixture is filtered in a Buchner funnel. The resulting filter cake is washed twice with 500 mL of de-ionized water at boiling temperature while stirring for 10 minutes, and then filtered after each washing step. Then the filter cake is washed three times with 100 mL of dried 2-propanol while in the Buchner funnel. Then, if necessary, the precipitate is mixed with 400 mL of dried 2-propanol and heated to reflux for 45 minutes and then filtered again before being extruded, as through a syringe. The extrudates are dried in a vacuum oven at 70.deg...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
Fractionaaaaaaaaaa
Fractionaaaaaaaaaa
Fractionaaaaaaaaaa
Login to view more

Abstract

A homogeneous ceria-based mixed-metal oxide, useful as a catalyst support, a co-catalyst and/or a getter, is described. The mixed-metal oxide has a relatively large surface area per weight, typically exceeding 150 m<2>/g, a structure of nanocrystallites having diameters of less than 4 nm, and including pores larger than the nanocrystallites and having diameters in the range of 4 to about 9 nm. The ratio of the pore volumes, VP, to skeletal structure volumes, VS, is typically less than about 2.5, and the surface area per unit volume of the oxide material is greater than 320 m<2>/cm<3>, such that the structural morphology supports both a relatively low internal mass transfer resistance and large effective surface area for reaction activity of interest. The mixed metal oxide is made by co-precipitating a dilute metal salt solution containing the respective metals, which may include Zr, Hf, and/or other metal constituents in addition to Ce, replacing water in the co-precipitate with a water-miscible low surface-tension solvent, and relatively quickly drying and calcining the co-precipitate at moderate temperatures. A highly dispersive catalyst metal, such as Pt, may be loaded on the mixed metal oxide support from a catalyst-containing solution following a selected acid surface treatment of the oxide support. The mixed metal oxide, as catalyst support, co-catalyst or getter, is applied in various reactions, and particularly water gas shift and/or preferential oxidation reactions as associated with fuel processing systems, as for fuel cells and the like.

Description

[0001] This invention relates to mixed metal oxides, and more particularly to ceria-based mixed-metal oxide structures, for use as catalyst supports, as co-catalysts, as getters, and the like. The invention relates further to methods of preparing such ceria-based mixed-metal oxide structures, and further still to metal loading of such structures. The invention relates still further to the application of such mixed-metal oxide structures as catalyst supports, co-catalysts, and / or getters in, for instance, fuel processing systems.[0002] Various metal oxides have found use in chemically reactive systems as catalysts, supports for catalysts, gettering agents and the like. As used herein, a gettering agent, or getter, is a substance that sorbs or chemically binds with a deleterious or unwanted impurity, such as sulfur. In those usages, their chemical characteristics and morphologies may be important, as well as their ease and economy of manufacture. One area of usage that is of particula...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): B01J23/00B01J23/10B01J23/20B01J23/28B01J23/36B01J23/63B01J23/656B01J32/00B01J35/10B01J37/03C01B3/16C01B3/48C01F17/241C01G25/00C01G27/00C01G33/00C01G39/00
CPCB01J23/002B01J23/10B01J23/63B01J23/6567B01J35/10B01J35/1019B01J35/1061B01J37/0036B01J37/03B01J2523/00B82Y30/00C01B3/16C01B2203/0283C01B2203/044C01B2203/066C01B2203/1064C01B2203/107C01B2203/1082C01F17/0043C01G25/00C01G25/006C01G27/006C01P2002/50C01P2002/52C01P2002/60C01P2002/72C01P2002/82C01P2006/12C01P2006/14C01P2006/16Y10T436/12B01J2523/3712B01J2523/48B01J2523/3706B01J2523/3718B01J2523/49B01J2523/375B01J2523/32B01J2523/74B01J2523/828B01J2523/56B01J2523/824B01J2523/68B01J2523/821B01J2523/3737B01J2523/827B01J2523/822Y02P20/52C01F17/241
Inventor VANDERSPURT, THOMAS HENRYWIJZEN, FABIENNETANG, XIALEFFLER, MIRIAM P.
Owner INT FUEL CELLS
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products