NOx control for IC engines

• US 20090004083A1
• Filed: 06/17/2005
• Published: 01/01/2009
• Est. Priority Date: 12/17/2003
• Status: Abandoned Application

• Current Assignee: Clean Diesel Technologies, Inc.
• Original Assignee: Clean Diesel Technologies, Inc.
• Inventors: Hofmann, John E., Peter-Hoblyn, Jeremy D., Valentine, James M.
• Application Number:
  US10/536,170
• Publication Number:
  US 20090004083A1
• Time in Patent Office: Days
• US Class Current: 423/239.200
• CPC Class Codes: B01D 2251/2062 Ammonia
• CPC Class Codes: B01D 2255/20715 Zirconium
• CPC Class Codes: B01D 2255/20723 Vanadium
• CPC Class Codes: B01D 2255/50 Zeolites
• CPC Class Codes: B01D 2257/404 Nitrogen oxides other than dinitrogen oxide
• CPC Class Codes: B01D 2258/012 Diesel engines and lean burn gasoline engines
• CPC Class Codes: F01N 13/0093 the purifying devices are of the same type
• CPC Class Codes: F01N 2570/14 Nitrogen oxides
• CPC Class Codes: F01N 2610/00 Adding substances to exhaust gases
• CPC Class Codes: F01N 3/2066 Selective catalytic reduction [SCR]
• CPC Class Codes: Y02T 10/12 Improving ICE efficiencies

Abstract

A multi-stage NOx reduction system employs catalysts effective at different temperature ranges and can have reagent injectors associated with each, for use in series or in parallel. A controller directs reagent introduction to one catalyst or the other as temperature and other conditions dictate. Valving can redirect exhaust to particular catalyst zones, if necessary.

Claims

1. A method for reducing the NO_x content of combustion exhaust comprising:

passing combustion gases through a multi-zone NO_x reduction catalytic treatment system, wherein reagent for NO_x reduction is introduced by means provided at least one point upstream of each catalyst zone.

2. A process according to claim 1 wherein a first catalyst zone is of the LT-1 or LT-2 type and a second stage catalyst is of the VNX or ZNX type.

3. A process according to claim 1 wherein, when the engine is operating under lower load conditions and the exhaust gas temperature is low, the NO_x reducing agent is injected upstream of catalyst zone 1, whereby reduction in NO_x emissions would be achieved over catalyst 1 and there would be little if any further reaction over catalyst 2.

4. A process according to claim 1 wherein, when the engine is operating at high load conditions, with relatively high gas temperatures, the continued injection of NO_x reducing reagent upstream of catalyst 1 is avoided where it can actually result in the formation of NO_x arising from the oxidation of the reagent and injection takes place in front of catalyst 2.

5. A process according to claim 1 wherein, an automatic sensor, based on gas temperature, provides a signal to a controller, which switches the location of reagent injection from zone 1 to zone 2 and reduction of NO_x is achieved over catalyst 1 or 2 whichever is most effective for NO_x reduction.

6. A process according to claim 1 wherein the gases are passed through a valve which directs exhaust gas flow to either low temperature catalyst No. 1 of the precious metal or base metal (e.g., vanadium/titanium) type during low exhaust gas temperatures (e.g., 350°

F.-800°

F.) such as described in SAE 2001-01-0519;

or to high temperature catalyst No. 2, typically of the zeolite type, for high temperatures (e.g., of 675°

F. to 1100°

F.) based on an input from a temperature sensor in the exhaust stream upstream of the exhaust gas valve.

7. A process according to claim 1 wherein reagent flow is done by one injector upstream of exhaust gas flow valve or after said valve but in front of each separate catalyst using two injectors one positioned in front of each catalyst.

8. A process according to claim 1 wherein exhaust gas flow is split between catalyst 1 and catalyst 2 for at least some portion of the engine operating cycle and reagent is injected upstream of each catalyst using a single injector upstream of the exhaust flow control valve or separate injectors in front of each catalyst.