EXHAUST PURIFICATION DEVICE AND METHOD OF CALCULATING NOx MASS REDUCED FROM LEAN NOx TRAP DURING REGENERATION

Patent metadata

Field	Value
Publication number	US-2016290197-A1
Application number	US-201514955955-A
Country	US
Kind code	A1
Filing date	Dec 1, 2015
Priority date	Mar 30, 2015
Publication date	Oct 6, 2016
Grant date	—

Abstract

A method of calculating a nitrogen oxide (NOx) mass reduced from a lean NOx trap (LNT) during regeneration includes calculating a C3H6 mass flow used to reduce the NOx among a C3H6 mass flow flowing into the LNT of an exhaust purification device, calculating a NH3 mass flow used to reduce the NOx among a NH3 mass flow generated in the LNT, calculating a reduced NOx mass flow based on the C3H6 mass flow used to reduce the NOx and the NH3 mass flow used to reduce the NOx, and calculating the reduced NOx mass by integrating the reduced NOx mass flow over a regeneration period.

First claim

What is claimed is:

1 . A method of calculating a nitrogen oxide (NOx) mass reduced from a lean NOx trap (LNT) during regeneration, comprising:
calculating a C3H6 mass flow used to reduce the NOx among a C3H6 mass flow flowing into the LNT of an exhaust purification device; calculating a NH3 mass flow used to reduce the NOx among a NH3 mass flow generated in the LNT; calculating a reduced NOx mass flow based on the C3H6 mass flow used to reduce the NOx and the NH3 mass flow used to reduce the NOx; and calculating the reduced NOx mass by integrating the reduced NOx mass flow over a regeneration period.

2 . The method of claim 1 , wherein the step of calculating the C3H6 mass flow used to reduce the NOx comprises:
calculating the C3H6 mass flow flowing into the LNT; calculating a used C3H6 mass flow by using the C3H6 mass flow flowing into the LNT, a NOx adsorption, a lambda at an upstream of the LNT, an LNT temperature, and a rich progress rate; and calculating the C3H6 mass flow used to reduce the NOx by using the used C3H6 mass flow.

3 . The method of claim 2 , wherein the step of calculating the NH3 mass flow used to reduce the NOx comprises:
calculating a mass flow of NH3 generated from C3H6 flowing into the LNT; calculating a total NH3 mass flow that is chemically reactable at the LNT; calculating a used NH3 mass flow by using the total NH3 mass flow that is chemically reactable at the LNT, the NOx adsorption, the lambda at the upstream of the LNT, the LNT temperature, and the rich progress rate; and calculating the NH3 mass flow used to reduce the NOx by using the used NH3 mass flow.

4 . The method of claim 3 , wherein the mass flow of the NH3 generated from the C3H6 flowing into the LNT is calculated according to the rich progress rate.

5 . The method of claim 2 , wherein the rich progress rate is defined as an equation of

1
-

λ
downstream

λ
upstream

2
-

λ
target

λ
target

,

wherein, λ target is a target lambda, λ upstream is the lambda at the upstream of the LNT, and λ downstream is a lambda at a downstream of the LNT.

6 . An exhaust purification device comprising:
an engine including an injector for injecting a fuel thereinto, generating power by burning a mixture of air and the fuel, and exhausting an exhaust gas generated during a combustion process to the exterior thereof through an exhaust pipe; a lean NOx trap (LNT) mounted on the exhaust pipe, for adsorbing nitrogen oxide (NOx) contained in the exhaust gas at a lean air/fuel ratio, releasing the adsorbed nitrogen oxide at a rich air/fuel ratio, and reducing the nitrogen oxide contained in the exhaust gas or the released nitrogen oxide using a reductant including carbon or hydrogen contained in the exhaust gas; and a controller for controling adsorption and release of the NOx by controlling an air/fuel ratio according to the NOx adsorbed in the LNT and a temperature of the exhaust gas, wherein the controller calculates a reduced NOx mass flow based on a C3H6 mass flow used to reduce the NOx among a C3H6 mass flow flowing into the LNT and a NH3 mass flow used to reduce the NOx among a NH3 mass flow generated in the LNT, and further calculates the NOx mass by integrating the reduced NOx mass flow over a regeneration period.

7 . The exhaust purification device of claim 6 , wherein the controller calculates the C3H6 mass flow used to reduce the NOx by using the C3H6 mass flow flowing into the LNT, a NOx adsorption, a lambda at an upstream of the LNT, an LNT temperature, and a rich progress rate.

8 . The exhaust purification device of claim 7 , wherein the controller calculates a mass flow of NH3 generated from C3H6 flowing into the LNT, calculates a total NH3 mass flow that is chemically reactabled at the LNT by using the mass flow of the NH3 generated from the C3H6, and calculates the NH3 mass flow used to reduce the NOx by using the total NH3 mass flow that is chemically reactable at the LNT, the NOx adsorption, the lambda at the upstream of the LNT, the LNT temperature, and the rich progress rate.

9 . The exhaust purification device of claim 8 , wherein the controller calculates the mass flow of the NH3 generated from the C3H6 flowing into the LNT is calculated according to the rich progress rate.

10 . The exhaust purification device of claim 7 , wherein the rich progress rate is defined as an equation of

1
-

λ
downstream

λ
upstream

2
-

λ
target

λ
target

,

wherein, λ target is a target lambda, λ upstream is the lambda at the upstream of the LNT, and A λ downstream is a lambda at a downstream of the LNT.

11 . The exhaust purification device of claim 6 , further comprising:
a dosing module mounted at the exhaust pipe downstream of the LNT for directly injecting a reducing agent into the exhaust gas; and a selective catalytic reduction (SCR) catalyst mounted at the exhaust pipe downstream of the dosing module for reducing the NOx contained in the exhaust gas by using the reducing agent injected by the dosing module, wherein the controller controls an amount of the reducing agent injected by the dosing module according to a NOx mass flow flowing into the SCR catalyst, and wherein the controller calculates a NH3 mass flow slipped from the LNT by using the total NH3 mass flow that is chemically reactable at the LNT, the NOx adsorption, the lambda at the upstream of the LNT, the LNT temperature, and the rich progress rate, and adjusts the amount of the reducing agent injected by the dosing module by considering the slipped NH3 mass flow.

Assignees

• Fev Gmbh
• Hyundai Motor Co Ltd

Inventors

• Lee Jin Ha
• Park Jin Woo
• Lim Sera
• Schaub Joschka
• Wittka Thomas
• Vovk Alexander

Classifications

• F02D2041/1433

  using a model or simulation of the system · CPC title

• F01N3/208

  Control of selective catalytic reduction [SCR], e.g. by adjusting the dosing of reducing agent · CPC title

• F01N2610/02

  the substance being ammonia or urea · CPC title

• F01N13/009

  having two or more separate purifying devices arranged in series · CPC title

• F01N3/0814 Primary

  combined with catalytic converters, e.g. NOx absorption/storage reduction catalysts · CPC title