SAE International SCR Catalyst Systems Optimized for Lightoff and Steady-State Performance 2009-01-0901

Description
A laboratory study was performed to optimize a zoned configuration of an iron (Fe) SCR catalyst and a copper (Cu) SCR catalyst in order to provide high NO x conversion at lean A/F ratios over a broad range of temperature for diesel and lean-burn gasoline applications. With an optimized space velocity of 8,300 hr 2x, a 67% (by volume) Fe section followed by a 33% Cu section provided at least 80% NO x conversion from approximately 230°C to 640°C when evaluated with 500 ppm NO and NH 3 . To improve the lean lightoff performance of the SCR catalyst system during a cold start, a Cu SCR catalyst that was 1/4 as long as the rear Cu SCR catalyst was placed in front of the Fe SCR catalyst. When evaluated with an excess of NH 3 (NH 3 /NO ratio of 2.2), the Cu+Fe+Cu SCR system had significantly improved lightoff performance relative to the Fe+Cu SCR system, although the front Cu SCR catalyst did decrease the NO x conversion at temperatures above 475°C by oxidizing some of the NH 3 to N 2 or NO.
Description
A laboratory study was performed to optimize a zoned configuration of an iron (Fe) SCR catalyst and a copper (Cu) SCR catalyst in order to provide high NO x conversion at lean A/F ratios over a broad range of temperature for diesel and lean-burn gasoline applications. With an optimized space velocity of 8,300 hr 2x, a 67% (by volume) Fe section followed by a 33% Cu section provided at least 80% NO x conversion from approximately 230°C to 640°C when evaluated with 500 ppm NO and NH 3 . To improve the lean lightoff performance of the SCR catalyst system during a cold start, a Cu SCR catalyst that was 1/4 as long as the rear Cu SCR catalyst was placed in front of the Fe SCR catalyst. When evaluated with an excess of NH 3 (NH 3 /NO ratio of 2.2), the Cu+Fe+Cu SCR system had significantly improved lightoff performance relative to the Fe+Cu SCR system, although the front Cu SCR catalyst did decrease the NO x conversion at temperatures above 475°C by oxidizing some of the NH 3 to N 2 or NO.

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SCR Catalyst Systems Optimized for Lightoff and Steady-State Performance - 2009-01-0901 - SAE International
Warrendale, PA, United States
SCR Catalyst Systems Optimized for Lightoff and Steady-State Performance
2009-01-0901
SCR Catalyst Systems Optimized for Lightoff and Steady-State Performance 2009-01-0901
A laboratory study was performed to optimize a zoned configuration of an iron (Fe) SCR catalyst and a copper (Cu) SCR catalyst in order to provide high NO x conversion at lean A/F ratios over a broad range of temperature for diesel and lean-burn gasoline applications. With an optimized space velocity of 8,300 hr 2x, a 67% (by volume) Fe section followed by a 33% Cu section provided at least 80% NO x conversion from approximately 230°C to 640°C when evaluated with 500 ppm NO and NH 3 . To improve the lean lightoff performance of the SCR catalyst system during a cold start, a Cu SCR catalyst that was 1/4 as long as the rear Cu SCR catalyst was placed in front of the Fe SCR catalyst. When evaluated with an excess of NH 3 (NH 3 /NO ratio of 2.2), the Cu+Fe+Cu SCR system had significantly improved lightoff performance relative to the Fe+Cu SCR system, although the front Cu SCR catalyst did decrease the NO x conversion at temperatures above 475°C by oxidizing some of the NH 3 to N 2 or NO.

A laboratory study was performed to optimize a zoned configuration of an iron (Fe) SCR catalyst and a copper (Cu) SCR catalyst in order to provide high NO x conversion at lean A/F ratios over a broad range of temperature for diesel and lean-burn gasoline applications. With an optimized space velocity of 8,300 hr 2x, a 67% (by volume) Fe section followed by a 33% Cu section provided at least 80% NO x conversion from approximately 230°C to 640°C when evaluated with 500 ppm NO and NH 3 . To improve the lean lightoff performance of the SCR catalyst system during a cold start, a Cu SCR catalyst that was 1/4 as long as the rear Cu SCR catalyst was placed in front of the Fe SCR catalyst. When evaluated with an excess of NH 3 (NH 3 /NO ratio of 2.2), the Cu+Fe+Cu SCR system had significantly improved lightoff performance relative to the Fe+Cu SCR system, although the front Cu SCR catalyst did decrease the NO x conversion at temperatures above 475°C by oxidizing some of the NH 3 to N 2 or NO.

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Technical Specifications

  SAE International
Product Category Standards and Technical Documents
Product Number 2009-01-0901
Product Name SCR Catalyst Systems Optimized for Lightoff and Steady-State Performance
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