Method and system for mitigating urea deposits within an SCR catalyst system

Patent metadata

Field	Value
Publication number	US-9718027-B2
Application number	US-201514808124-A
Country	US
Kind code	B2
Filing date	Jul 24, 2015
Priority date	Jul 13, 2012
Publication date	Aug 1, 2017
Grant date	Aug 1, 2017

Abstract

A method and system for mitigating a urea deposit within an SCR system that includes determining a mass of an accumulated urea deposit present within the SCR catalyst and SCR piping, comparing the mass of the accumulated urea deposit with a deposit upper threshold limit, and initiating an SCR regeneration event when the mass of the accumulated urea deposit is greater than the deposit upper threshold limit. The method further includes determining an amount of NH 3 passing through the SCR catalyst downstream of the urea deposit, comparing the amount of NH 3 passing through the SCR catalyst with an NH 3 regeneration threshold limit, and terminating the SCR regeneration event when the level of NH 3 passing through the SCR catalyst is less than the SCR NH 3 regeneration threshold.

First claim

What is claimed is:

1. A method for mitigating a urea deposit within a selective catalytic reduction (SCR) system in exhaust receiving communication with an exhaust gas stream produced by an engine system, the exhaust gas stream flowing from an engine of the engine system to a tailpipe of the engine system, the method comprising:
determining a mass of an accumulated urea deposit present within a SCR system, the SCR system including a SCR catalyst and SCR piping;
comparing the mass of the accumulated urea deposit with a deposit upper threshold limit;
initiating a SCR regeneration event when the mass of the accumulated urea deposit is greater than the deposit upper threshold limit;
determining an amount of NH 3 passing through the SCR system downstream of the urea deposit;
comparing the amount of NH 3 passing through the SCR system with an NH 3 regeneration threshold limit; and
terminating the SCR regeneration event when the amount of NH 3 passing through the SCR system is less than the SCR NH 3 regeneration threshold, the SCR NH 3 regeneration threshold based on a decomposition rate of the mass of the accumulated urea deposit, the decomposition rate based on an exhaust gas temperature.

2. The method of claim 1 , wherein determining the mass of an accumulated urea deposit comprises:
determining a rate of urea deposit accumulation within the SCR system;

determining a first time period, the first time period being the time elapsed from a previous SCR regeneration event; and
integrating the rate of urea deposit accumulation within the SCR system over the first time period to calculate the mass of the accumulated urea deposit.

3. The method of claim 1 , wherein determining the amount of NH3 passing through the SCR system downstream of the urea deposit comprises:
determining a flow rate of NH 3 passing through the SCR system downstream of the urea deposit;
determining a second time period, the second time period being the time elapsed from the initiation of the SCR regeneration event; and
integrating the rate of NH 3 passing through the SCR system over the second time period to calculate the amount of NH 3 passing through the SCR system.

4. The method of claim 3 , further comprising measuring the flow rate of NH 3 passing through the SCR system with a virtual NH 3 sensor.

5. The method of claim 3 , further comprising measuring the flow rate of NH 3 passing through the SCR system with an NH 3 sensor positioned downstream of the urea deposit.

6. The method of claim 5 , wherein the NH 3 sensor is a SCR catalyst NH 3 mid-bed sensor.

7. A method for mitigating a urea deposit within a selective catalytic reduction (SCR) system in exhaust receiving communication with an exhaust gas stream produced by an engine system, the exhaust gas stream flowing from an engine of the engine system to a tailpipe of the engine system, the method comprising:
determining a mass of an accumulated urea deposit present within the SCR system, the SCR system including a SCR catalyst and SCR piping upstream of the SCR catalyst;
comparing the mass of the accumulated urea deposit with a deposit upper threshold limit;
initiating a SCR regeneration event when the mass of the accumulated urea deposit is greater than the deposit upper threshold limit;
determining an amount of NH 3 passing through the SCR catalyst downstream of the urea deposit;
comparing the amount of NH 3 passing through the SCR catalyst with an NH 3 regeneration threshold limit;
maintaining the SCR regeneration event when the level of NH 3 passing through the SCR catalyst is greater than the NH 3 regeneration threshold limit;
comparing the mass of the accumulated urea deposit with a deposit lower threshold limit; and
terminating the SCR regeneration event when the mass of the accumulated urea deposit is less than the deposit lower threshold limit, the deposit lower threshold limit based on a decomposition rate of the mass of the accumulated urea deposit, the decomposition rate based on an exhaust gas temperature.

8. The method of claim 7 , wherein determining the mass of the accumulated urea deposit comprises:
determining a rate of urea deposit accumulation within the SCR system;

determining a first time period, the first time period being the time elapsed from a previous SCR regeneration event; and
integrating the rate of urea deposit accumulation within the SCR system over the first time period to calculate the mass of the accumulated urea deposit.

9. The method of claim 7 , wherein determining the amount of NH 3 passing through the SCR catalyst downstream of the urea deposit comprises:
determining a flow rate of NH 3 passing through the SCR catalyst downstream of the urea deposit;
determining a second time period, the second time period being the time elapsed from the initiation of the SCR regeneration event; and
integrating the rate of NH 3 passing through the SCR catalyst over the second time period to calculate the amount of NH 3 passing through the SCR catalyst.

10. The method of claim 9 , further comprising measuring the flow rate of NH 3 passing through the SCR catalyst downstream of the urea deposit with a virtual NH 3 sensor.

11. The method of claim 9 , further comprising measuring the flow rate of NH 3 passing through the SCR catalyst downstream of the urea deposit with an NH 3 sensor positioned downstream of the urea deposit.

12. The method of claim 11 , wherein determining the mass of the accumulated urea deposit comprises:
determining a rate of urea deposit decomposition within the SCR system; and
integrating the rate of urea deposit decomposition within the SCR system over the second time period to calculate the mass of the accumulated urea deposit.

Assignees

• Cummins Ip Inc

Inventors

• Zeng Fan
• Bruner C Larry
• Hodzen Edmund P
• Package Ian A
• Kumar Shankar
• Kamasamudram Krishna

Classifications

• B01D53/9404

  Removing only nitrogen compounds · CPC title

• F01N2900/1806

  Properties of reducing agent or dosing system · 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

• F01N3/2066 Primary

  Selective catalytic reduction [SCR] · CPC title

• B01D53/9495 Primary

  Controlling the catalytic process · CPC title