After treatment system and after treatment method for lean-burn engine

Patent metadata

Field	Value
Publication number	US-2020248608-A1
Application number	US-201916263615-A
Country	US
Kind code	A1
Filing date	Jan 31, 2019
Priority date	Jan 31, 2019
Publication date	Aug 6, 2020
Grant date	—

Abstract

An after treatment method for a lean-burn engine is disclosed. The after treatment method is configured to control an after treatment system sequentially equipped with an ammonia production catalyst module, a selective catalytic reduction (SCR) catalyst, and a CO clean-up catalyst (CUC) on an exhaust pipe through which an exhaust gas flows and which is connected to a lean-burn engine. In the after treatment method, a rich air/fuel ratio (AFR) is controlled in multiple phases in response to detecting that conversion to the rich AFR is desired.

First claim

What is claimed is:

1 . An after treatment system for a lean-burn engine, comprising:
an exhaust pipe connected to the lean-burn engine and through which an exhaust gas generated in the lean-burn engine flows; an ammonia production catalyst module mounted on the exhaust pipe, capable of purifying emission contained in the exhaust gas, and generating ammonia (NH 3 ) using nitrogen oxide (NOx) contained in the exhaust gas or NOx stored therein at a rich air/fuel ratio (AFR); a selective catalytic reduction (SCR) catalyst mounted on the exhaust pipe downstream of the ammonia production catalyst module, storing the NH 3 generated in the ammonia production catalyst module, and reducing the NOx contained in the exhaust gas using the stored NH 3 ; a CO clean-up catalyst (CUC) mounted on the exhaust pipe downstream of the SCR catalyst and purifying CO contained in the exhaust gas; and a controller detecting information on the AFR and temperature of the exhaust gas and controlling the AFR of the exhaust gas based on the information on the AFR and the temperature of the exhaust gas, wherein, in response to detecting information that the rich AFR is desirable, the controller is configured to sequentially perform a rich control of first phase in which consumption of oxygen storage capacity (OSC) in the ammonia production catalyst module is accelerated, a rich control of second phase in which the OSC is completely consumed, and a rich control of third phase in which the NH 3 is generated before the CO is slipped from the CUC.

2 . The after treatment system of claim 1 , wherein the AFR is controlled to be a first AFR in the rich control of first phase, the AFR is controlled to be a second AFR in the rich control of second phase, and the AFR is controlled to be a third AFR in the rich control of third phase.

3 . The after treatment system of claim 2 , wherein the first AFR is greater than the second AFR, and the second AFR is greater than the third AFR based on a detected value of an oxygen sensor mounted at an upstream of the ammonia production catalyst module.

4 . The after treatment system of claim 2 , wherein the controller further performs a rich control of fourth phase in which the NH3 is further generated to a rich duration at which a slip amount of the CO accumulated downstream of the CUC reaches a predetermined amount.

5 . The after treatment system of claim 4 , wherein the AFR is controlled to be a fourth AFR in the rich control of fourth phase, and
wherein the fourth AFR is greater than the first AFR to the third AFR based on a detected value of an oxygen sensor mounted at an upstream of the ammonia production catalyst module.

6 . The after treatment system of claim 5 , wherein the rich duration is calculated according to the fourth AFR and a temperature of the CUC.

7 . The after treatment system of claim 2 , wherein the rich control of first phase is performed for a predetermined duration.

8 . The after treatment system of claim 7 , wherein the predetermined duration is calculated according to the OSC and the first AFR.

9 . The after treatment system of claim 1 , wherein the ammonia production catalyst module comprises:
a three-way catalyst (TWC) purifying hydrocarbon (HC), the CO, and the NOx contained in the exhaust gas; and an ammonia production catalyst (APC) mounted on the exhaust pipe downstream of the TWC, storing the NOx at a lean AFR, and generating H 2 , releasing the stored NOx, and generating the NH 3 using the released NOx and the generated H 2 at the rich AFR.

10 . The after treatment system of claim 9 , further comprising a particulate filter disposed between the TWC and the APC or between the APC and the SCR catalyst,
wherein the particulate filter traps particulate matter in the exhaust gas.

11 . An after treatment method for controlling an after treatment system sequentially equipped with an ammonia production catalyst module, a selective catalytic reduction (SCR) catalyst, and a CO clean-up catalyst (CUC) on an exhaust pipe through which an exhaust gas flows and which is connected to a lean-burn engine, the after treatment method comprising:
operating the engine at a lean AFR; calculating an amount of NH 3 stored in the SCR catalyst; determining whether conversion to a rich AFR is desired; operating, when the conversion to the rich AFR is desired, the engine at a first AFR for a predetermined duration; and operating the engine at a second AFR until oxygen storage capacity (OSC) in the ammonia production catalyst module is completely consumed.

12 . The after treatment method of claim 11 , wherein the first AFR is less than the second AFR based on a detected value of an oxygen sensor mounted at an upstream of the ammonia production catalyst module.

13 . The after treatment method of claim 11 , wherein the predetermined duration is calculated according to the OSC and the first AFR.

14 . The after treatment method of claim 11 , further comprising operating the engine at a third AFR before CO is slipped from the CUC.

15 . The after treatment method of claim 14 , wherein the third AFR is greater than the second AFR based on a detected value of an oxygen sensor mounted at an upstream of the ammonia production catalyst module.

16 . The after treatment method of claim 14 , further comprising operating the engine at a fourth AFR to a rich duration at which a slip amount of the CO accumulated downstream of the CUC reaches a predetermined amount.

17 . The after treatment method of claim 16 , wherein the fourth AFR is greater than the first AFR to the third AFR based on a detected value of an oxygen sensor mounted at an upstream of the ammonia production catalyst module.

18 . The after treatment method of claim 16 , wherein the rich duration is calculated according to the fourth AFR and a temperature of the CUC.

19 . The after treatment method of claim 11 , wherein the determining whether conversion to a rich AFR is desired includes calculating an amount of NOx which will flow into the SCR catalyst, and
wherein the conversion to the rich AFR is determined to be desired when the amount of the NH 3 stored in the SCR catalyst is smaller than an amount of the NH 3 required to purify the amount of the NOx which will flow into the SCR catalyst.

20 . The after treatment method of claim 11 , wherein the determining whether conversion to a rich AFR is desired includes comparing the amount of the NH 3 stored in the SCR catalyst with a predetermined NH 3 lower threshold, and
wherein the conversion to the rich AFR is determined to be desired when the amount of the NH 3 stored in the SCR catalyst is smaller than the predetermined NH 3 lower threshold.

Assignees

• Hyundai Motor Co Ltd
• Kia Motors Corp

Inventors

• Joo Nahm Roh
• Jung Changho
• Kim Chang Hwan
• Yi Seung Jae

Classifications

• Y02A50/20

  Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters · CPC title

• F01N3/0842

  Nitrogen oxides · CPC title

• F01N9/00

  Electrical control of exhaust gas treating apparatus (monitoring or diagnostic devices for exhaust-gas treatment apparatus F01N11/00; conjoint electrical control of two or more combustion engine functions F02D43/00) · CPC title

• F01N2570/10

  Carbon or carbon oxides · CPC title

• F01N2900/1624

  Catalyst oxygen storage capacity · CPC title