Exhaust purification system and method of desulfurizing lean NOx trap of exhaust purification system provided with lean NOx trap and selective catalytic reduction catalyst

Patent metadata

Field	Value
Publication number	US-10287944-B2
Application number	US-201514955858-A
Country	US
Kind code	B2
Filing date	Dec 1, 2015
Priority date	Aug 25, 2015
Publication date	May 14, 2019
Grant date	May 14, 2019

Abstract

A method of desulfurizing a lean NOx trap (LNT) of an exhaust purification system provided with the LNT and a selective catalytic reduction (SCR) catalyst includes determining whether a desulfurization feasibility condition of the LNT is satisfied, determining whether a desulfurization demand condition of the LNT is satisfied, and performing desulfurization of the LNT if both of the desulfurization feasibility condition of the LNT and the desulfurization demand condition of the LNT are satisfied, wherein the desulfurization of the LNT is performed by repeating a desulfurization lean mode and a desulfurization rich mode according to whether a mode switching condition due to a desulfurization temperature is satisfied and whether a mode switching condition due to generation of H2S is satisfied.

First claim

What is claimed is:

1. A method of desulfurizing a lean NOx trap (LNT) of an exhaust purification system provided with the LNT and a selective catalytic reduction (SCR) catalyst, the method comprising:
determining whether a desulfurization feasibility condition of the LNT is satisfied;
determining whether a desulfurization demand condition of the LNT is satisfied; and
performing desulfurization of the LNT if both of the desulfurization feasibility condition of the LNT and the desulfurization demand condition of the LNT are satisfied,
wherein the desulfurization of the LNT is performed by repeating a desulfurization lean mode and a desulfurization rich mode according to whether a mode switching condition due to a desulfurization temperature is satisfied and whether a mode switching condition due to generation of H2S is satisfied,
wherein the mode switching condition due to the desulfurization temperature is satisfied when a lean mode condition due to the desulfurization temperature or a rich mode condition due to the desulfurization temperature is satisfied based on a temperature state above a target window, a temperature state below the target window, whether a delay time condition is satisfied, an engine operation mode and sign of a temperature difference between the desulfurization lean mode and the desulfurization rich mode.

2. The method of claim 1 , wherein the temperature state above the target window and the temperature state below the target window are determined based on a temperature controllable state, a temperature at a downstream of the LNT, an engine speed and an engine torque.

3. The method of claim 1 , wherein the delay time condition is satisfied when (1) the engine operation mode is the desulfurization rich mode or the desulfurization lean mode, (2) the engine operation mode continues for a predetermined delay, and satisfaction of the conditions (1) and (2) continues for a delay time.

4. The method of claim 3 , wherein the delay time is calculated based on an absolute value of the temperature difference between the desulfurization lean mode and the desulfurization rich mode and a mass flow of an exhaust gas.

5. The method of claim 1 , wherein the mode switching condition due to generation of H2S is satisfied when a rich mode condition due to generation of H2S or a lean mode condition due to generation of H2S is satisfied.

6. The method of claim 5 , wherein the rich mode condition due to generation of H2S is satisfied when a temperature uncontrollable state is output, the engine operation mode is the desulfurization lean mode, and a time for which the engine operation mode is the desulfurization lean mode is longer than or equal to a final target lean period.

7. The method of claim 6 , wherein the final target lean period is calculated based on a base lean period according to an accumulated time for which the engine operation mode was the desulfurization rich mode in the past and a lean period correction factor according to the mass flow of the exhaust gas and a difference between a target temperature and an actual temperature.

8. The method of claim 5 , wherein the lean mode condition due to generation of H2S is satisfied when the engine operation mode is the desulfurization rich mode, and a time for which the engine operation mode is the desulfurization rich mode is longer than or equal to a period selected from the group consisting of a target maximum rich mode period and a lambda synchronization delay time has passed since a lambda sensor synchronization signal was input.

9. The method of claim 8 , wherein the target maximum rich mode period is calculated based on a base rich period according to the temperature at the downstream of the LNT and a sulfur poisoning in the LNT, and a rich period correction factor according to an O2 adsorption in the LNT and an upstream lambda.

10. The method of claim 8 , wherein the lambda synchronization delay time is calculated according to an upstream lambda.

11. The method of claim 1 , wherein the desulfurization feasibility condition of the LNT is satisfied when an engine operation point condition, a temperature threshold condition for desulfurization, an engine operation mode condition, a vehicle speed condition and a soot load condition are satisfied and a desulfurization break condition is not satisfied.

12. The method of claim 1 , wherein the desulfurization demand condition of the LNT is satisfied if any one of a desulfurization beneficial condition, a DPF regeneration completion condition and a sulfur load condition is satisfied.

13. The method of claim 12 , wherein the desulfurization beneficial condition is satisfied if a ratio of a current sulfur load to a maximum sulfur load is larger than or equal to a threshold sulfur load ratio, the average temperature of the LNT is higher than or equal to a minimum average temperature of the LNT for desulfurization, and a current vehicle speed is between a maximum desulfurization vehicle speed and a minimum desulfurization vehicle speed.

14. The method of claim 13 , wherein the threshold sulfur load ratio is calculated according to a desulfurization beneficial factor, and
wherein the desulfurization beneficial factor is calculated based on a desulfurization condition state, the vehicle travel distance and an engine operation duration.

15. The method of claim 13 , wherein the minimum average temperature of the LNT for desulfurization is calculated according to the ratio of the current sulfur load to the maximum sulfur load.

16. The method of claim 15 , wherein the maximum sulfur load is calculated by multiplying a maximum sulfur load per volume according to the aging factor of the LNT to a volume of the LNT.

17. The method of claim 12 , wherein the DPF regeneration completion condition is satisfied if the engine operation mode is a DPF regeneration mode, the soot load condition is satisfied, and the ratio of the current sulfur load to the maximum sulfur load is larger than or equal to a minimum sulfur load ratio.

18. The method of claim 12 , wherein the desulfurization demand condition of the LNT is not satisfied if a desulfurization reset condition is satisfied, and
wherein the desulfurization reset condition is satisfied if a desulfurization break condition is satisfied, a sulfur load in the LNT is smaller than or equal to a desulfurization reset sulfur load, or a duration for which the engine operation mode is the desulfurization rich mode is longer than or equal to a desulfurization rich demand duration.

Assignees

• Hyundai Motor Co Ltd
• Fev Gmbh

Inventors

• Lee Jin Ha
• Park Won Soon
• Park Jin Woo
• Joo Ki Hyung
• Lim Sera
• Wittka Thomas
• Vovk Alexander
• Schaub Joschka

Classifications

• B01J20/3085

  Chemical treatments not covered by groups B01J20/3007 - B01J20/3078 · CPC title

• B01D53/9422

  for removing nitrogen oxides by NOx storage or reduction by cyclic switching between lean and rich exhaust gases (LNT, NSC, NSR) · CPC title

• B01D53/9495

  Controlling the catalytic process · CPC title

• B01D2257/304

  Hydrogen sulfide · CPC title

• F01N3/2066 Primary

  Selective catalytic reduction [SCR] · CPC title