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NOx adsorber aftertreatment system for internal combustion engines

an aftertreatment system and nox technology, applied in the field of internal combustion engines, can solve problems such as temperature rise, and achieve the effects of increasing temperature, reducing the amount of nox adsorber, and increasing the time and surface area

Inactive Publication Date: 2007-08-02
MITAL RAHUL +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0011] In one embodiment, a catalytic soot filter is positioned upstream from the adsorber. The additional hydrocarbon used to promote regeneration is injected into the catalytic soot filter. The catalytic soot filter, when used in combination with the adsorber, provides more time and surface area for the hydrocarbon to react with the oxygen. The catalytic soot filter will additionally reformulate some of the diesel fuel into hydrogen and carbon monoxide, which have been shown to be better reductants than diesel fuel.
[0012] In another embodiment, a catalytic soot filter is positioned downstream from the adsorber. The heat generated by the regenerating adsorber is transferred downstream to the soot filter, thereby heating the soot filter above the temperature required for regeneration. Additionally, any hydrocarbon that slips through the adsorber is burned in the catalytic soot filter, further raising the temperature. Such burning of the hydrocarbon slip in the catalytic soot filter obviates the need for a diesel oxidation catalyst, thereby reducing system cost and package size.

Problems solved by technology

Additionally, any hydrocarbon that slips through the adsorber is burned in the catalytic soot filter, further raising the temperature.

Method used

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fourth embodiment

[0050] As discussed hereinabove, catalytic soot filters 18 require high temperatures in order to regenerate. It is difficult to attain these high temperatures in the exhaust stream during low load operation of the engine 12. Under these conditions, the soot filter 18 eventually becomes clogged with soot. By placing the soot filter 18 upstream from the adsorber 26 and downstream from the fuel injector 30 as shown in the fourth embodiment, the catalytic soot filter 18 also receives the injected hydrocarbon and is regenerated by combustion of this hydrocarbon. Placement of the catalytic soot filter 18 in this position also provides more time and surface area for the introduced hydrocarbon to react with oxygen, thereby more completely burning the hydrocarbon. More complete hydrocarbon combustion will possibly eliminate the need for the diesel oxidation catalyst 40, thereby reducing exhaust system cost and package size.

[0051] Furthermore, the catalytic soot filter 18 will reformulate som...

fifth embodiment

[0053] As discussed hereinabove, catalytic soot filter 18 requires high temperatures in order to regenerate. It is difficult to attain these high temperatures in the exhaust stream during low load operation of the engine 12. Under these conditions, the soot filter 18 eventually becomes clogged with soot. By placing the soot filter 18 downstream from the adsorber 26 as shown in the fifth embodiment, heat generated in the adsorber 26 due to the combustion of the introduced hydrocarbon serves to raise the temperature of the catalytic soot filter 18 sufficiently to accomplish regeneration.

[0054] Furthermore, any hydrocarbon that slips unburned through the adsorber 26 will oxidize in the soot filter 18, thereby generating further heat to encourage regeneration of the soot filter 18. Because the hydrocarbon slip is oxidized in the soot filter 18, the diesel oxidation catalyst 40 of the prior embodiments is no longer required. Elimination of the diesel oxidation catalyst 40 reduces the exh...

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Abstract

The present invention provides for an NOx adsorber aftertreatment system for internal combustion engines which utilizes a parallel arrangement of an adsorber catalyst and a bypass. The exhaust flow from the engine is routed through the adsorber during lean operation. At a predetermined regeneration time (for example, when the adsorber catalyst is 20% full), the exhaust gas flow is reduced through the parallel leg that contains the adsorber catalyst to be regenerated (e.g., 20% through the catalyst leg, 80% of the flow to the bypass leg). A quantity of hydrocarbon is injected into the reduced-flow catalyst leg in order to make the mixture rich. Since the flow has been reduced in this leg, only a small fraction of the amount of hydrocarbon that would have been required to make the mixture rich during full flow is required. This will result in a substantial reduction in the fuel penalty incurred for regeneration of the adsorber catalyst. Once the leg has been regenerated, the exhaust flow is switched to flow 100% through the adsorber leg.

Description

TECHNICAL FIELD OF THE INVENTION [0001] The present invention generally relates to internal combustion engines and, more particularly, to an NOx adsorber aftertreatment system for internal combustion engines. BACKGROUND OF THE INVENTION [0002] As environmental concerns have led to increasingly strict regulation of engine emissions by governmental agencies, reduction of nitrogen-oxygen compounds (NOx) in exhaust emissions from internal combustion engines has become increasingly important. Current indications are that this trend will continue. [0003] Future emission levels of diesel engines will have to be reduced in order to meet Environmental Protection Agency (EPA) regulated levels. In the past, the emission levels of U.S. diesel engines have been regulated according to the EPA using the Federal Test Procedure (FTP) cycle, with a subset of more restrictive emission standards for California via the California Air Resources Board (CARB). For example, the Tier II emission standards, w...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): F01N3/00B01D53/96F01N3/035F01N3/08F01N3/36F01N3/38F01N13/02F01N13/04
CPCB01D53/96F01N13/011F01N3/0814F01N3/0821F01N3/0842F01N3/085F01N3/0871F01N3/0878F01N3/36F01N3/38F01N9/00F01N2250/02F01N2250/12F01N2250/14F01N2410/12F01N2570/04F01N2570/14F01N2610/03F01N2610/14Y02T10/47F01N13/009F01N3/035Y02T10/40Y02A50/20
Inventor MITAL, RAHULSTROIA, BRADLEE J.COLE, SCOTT
Owner MITAL RAHUL
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