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Zeolite-Containing Oxidation Catalyst and Method of Use

a technology of oxidation catalyst and zeolite, which is applied in the direction of physical/chemical process catalyst, domestic stove or range, separation process, etc., can solve the problems of less effective catalysts used to treat the exhaust of internal combustion engines during periods of relatively low temperature operation

Inactive Publication Date: 2007-08-30
YAVUZ BULENT O +4
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0009] Generally, in accordance with the present invention, there is provided a catalyst composition and a method for oxidizing oxidizeable components of diesel engine exhaust in which at least some of a volatile organic fraction of the diesel exhaust is converted to innocuous materials, and in which gaseous HC and CO pollutants may also be similarly converted. The objectives of the invention are attained by an oxidation catalyst comprising a catalytic material comprising a mixture of high surface area ceria, a zeolite and, optionally, a high surface area alumina. The catalytic material optionally may carry a low loading of platinum catalytic metal dispersed thereon or palladium catalytic metal dispersed thereon. Alternatively, or in addition, the zeolite of the catalyst composition may be doped, e.g., ion-exchanged, with a catalytic moiety such as one or more of hydrogen ion, platinum, copper, nickel, cobalt, iron, etc. The method of the invention is attained by flowing a diesel engine exhaust, e.g., the exhaust of a diesel-powered automobile or light truck, into contact under oxidation reaction conditions with a catalyst composition as described above.

Problems solved by technology

One problem faced in the treatment of diesel engine exhaust is presented by the presence of sulfur in diesel fuel.
As is well-known in the art, catalysts used to treat the exhaust of internal combustion engines are less effective during periods of relatively low temperature operation, such as the initial cold-start period of engine operation, because the engine exhaust is not at a temperature sufficiently high for efficient catalytic conversion of noxious components in the exhaust.

Method used

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  • Zeolite-Containing Oxidation Catalyst and Method of Use
  • Zeolite-Containing Oxidation Catalyst and Method of Use
  • Zeolite-Containing Oxidation Catalyst and Method of Use

Examples

Experimental program
Comparison scheme
Effect test

example a

Preparation of Fe-Beta Zeolite

[0056] To prepare a sample of iron-exchanged Beta zeolite (Fe-Beta zeolite), 17 grams of iron [II] sulfate was dissolved in 800 ml water. One hundred grams of Beta zeolite was added to the solution which was then stirred for 1 hour at a temperature of 70° C. to 80° C. The resulting slurry was then filtered and washed with 2 liters of water, dried at 120° C. and calcined at 540° C. The resulting material comprised 1.65% by weight iron. This technique was employed to prepare the Fe-Beta zeolite catalysts used in the following Examples.

example b

Preparation of Pt—Fe-Beta Zeolite

[0057] A solution was prepared using 0.54 grams of tetraammine platinum chloride in 500 ml water, to which 100 grams of Beta zeolite was added. The mixture was stirred for 24 hours at room temperature so that platinum ions replaced sodium ions in the zeolite material. The slurry was then filtered and washed with 2 liters water, dried and calcined at 540° C. The resulting calcined, platinum ion-exchanged Beta zeolite was then ion-exchanged with iron [II] sulfate by adding the zeolite to a solution of iron [III] sulfate equivalent to 17 grams of iron [II] sulfate in 800 ml water. The solution was allowed to stand for about 1 hour and was then stirred at 70° C. to 80° C. for 1 hour. The resulting slurry was then filtered, washed with water, dried at 120° C. and calcined at 540° C. On a dry basis, the Beta zeolite comprised 1.6% by weight iron and 0.25% by weight platinum. This technique was employed to prepare the Fe—Pt-Beta zeolite catalyst components...

example 1

[0058] A. A catalyst according to the present invention was prepared by coating a honeycomb monolith with a catalytic material comprised of a zeolite, bulk ceria and bulk alumina to provide 0.84 g / in3 gamma-alumina, 0.83 g / in3 alumina-stabilized ceria and 0.83 g / in3 Fe-Beta zeolite. The honeycomb monolith was a cordierite substrate measuring 9 inches in diameter by 6 inches long and having 4.00 cpsi. The catalyst material also provided 2.5 g / ft3 of platinum, 80 percent by weight of which was dispersed on the alumina, and 20 percent by weight of which was dispersed on the ceria. This catalyst was designated E-1.

[0059] B. For comparison, three other catalysts were prepared to provide a series of three otherwise identical compositions containing a ceria-alumina catalytic material but no zeolite and, in two cases, having platinum dispersed thereon. The platinum loadings of these comparative catalysts were 0.0, 0.5 and 2.0 g / ft3 platinum. Each comparative catalyst comprised a gamma-alum...

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Abstract

Oxidation catalyst compositions for treating diesel exhaust include ceria and, optionally, alumina, each having a surface area of at least about 10 m2 / g, and a zeolite, e.g., Beta zeolite. Optionally, platinum may be included in the catalytic material, preferably in amounts which are sufficient to promote some gas-phase oxidation of carbon monoxide (“CO”) and hydrocarbons (“HC”) but which are limited to preclude excessive oxidation of SO2 to SO3. Alternatively, palladium in any desired amount may be included in the catalytic material. The zeolite is optionally doped, e.g., ion-exchanged, with one or more of hydrogen, a platinum group metal or other catalytic metals. The catalyst compositions may be used in a method to treat diesel engine exhaust by contacting the hot exhaust with the catalyst composition to promote the oxidation of gas-phase CO and HC and of the volatile organic fraction component of particulates in the exhaust.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS [0001] This application is a continuation of application Ser. No. 11 / 043,613, filed Jan. 26, 2005, which is a continuation of application Ser. No. 09 / 880,375, filed on Jun. 13, 2001, now abandoned, which is a continuation of application Ser. No. 08 / 458,052, filed Jun. 1, 1995, now U.S. Pat. No. 6,274,107, which is a division of application Ser. No. 08 / 255,289, filed Jun. 7, 1994, now U.S. Pat. No. 6,248,684, which is a continuation of application Ser. No. 08 / 038,378, filed Mar. 29, 1993, now abandoned, which is a continuation-in-part of application Ser. No. 07 / 973,461, filed Nov. 19, 1992, now abandoned.BACKGROUND OF THE INVENTION [0002] 1. Field of the Invention [0003] This invention relates to a catalyst composition and method for the oxidation of oxidizeable components of diesel engine exhaust, and more specifically to the treatment of such diesel exhaust to reduce the content of particulates and other pollutants discharged to the atmospher...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): F01N3/00B01D53/86B01D53/94B01J23/10B01J23/63B01J29/72B01J35/10B01J37/02F02B3/06F24C15/20
CPCB01D53/864F02B3/06B01D53/9481B01D2255/102B01D2255/206B01D2255/20723B01D2255/20738B01D2255/20753B01D2255/20761B01D2255/50B01D2255/912B01D2255/9207B01J23/10B01J23/63B01J29/7215B01J29/7615B01J35/0006B01J35/10B01J37/0215B01J37/0244B01J37/0246B01J37/0248F01N2510/06F01N2510/063F01N2510/0682F01N2510/0684B01D53/944B01J35/023B01J35/1014B01J35/1019Y02A50/20
Inventor YAVUZ, BULENT O.VOSS, KENNETH E.DEEBA, MICHELADOMAITIS, JOHN R.FARRAUTO, ROBERT J.
Owner YAVUZ BULENT O
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