SCR Catalyst Degradation Estimation via Segmented Temperature Modeling

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing SCR catalyst degradation models in aftertreatment systems for compression ignition engines are simplistic and fail to account for real-time noise factors, leading to inadequate identification of degradation in individual vehicles or sub-groups, which complicates emissions control and maintenance.

Innovation Solution

A physics-based cumulative damage model that uses real-time engine-aftertreatment data to estimate SCR catalyst degradation, incorporating parameters like temperature, ammonia slip, and population damage signals to adjust reductant and hydrocarbon dosing, and trigger preventive maintenance alerts.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Device complexity

If a simplistic degradation model is used, then device complexity is reduced, but measurement precision and reliability of degradation detection deteriorate

Engineering Contradiction:
Improvedegradation model complexityVSAvoiddegradation detection precision
Core Design Contradiction:
Device complexityVSMeasurement precision

Solution Approach 1:

The degradation model is segmented into two distinct components: a short-term cumulative degradation model capturing reversible effects from sulfur and hydrocarbons, and a long-term cumulative degradation model capturing irreversible thermal aging. This segmentation allows each model to focus on specific degradation mechanisms, improving detection precision while keeping individual model complexities manageable.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The model incorporates dynamic parameter changes by using real-time SCR catalyst temperature as a key input variable that modulates the degradation rates. The temperature-dependent degradation rates allow the model to adapt to varying operating conditions, improving measurement precision without requiring an excessively complex structural framework.

Inventive Principle:
Principle #35Parameter changes

2Reliability

If real-time degradation monitoring is implemented, then emissions control reliability is improved, but use of energy and computational resources increases

Engineering Contradiction:
Improveemissions control reliabilityVSAvoidcomputational energy consumption
Core Design Contradiction:
ReliabilityVSUse of energy by moving object

Solution Approach 1:

The system implements continuous feedback by monitoring real-time SCR catalyst temperature and using it to dynamically adjust the degradation estimates. This feedback mechanism allows the controller to reliably track catalyst health and adjust reductant dosing accordingly, while the feedback loop remains computationally efficient by focusing on the most influential parameter (temperature) rather than processing all possible operating parameters.

Inventive Principle:
Principle #23Feedback

Solution Approach 2:

The degradation model serves itself by using readily available sensor data (SCR catalyst temperature) that is already collected for other control purposes. This self-service approach allows the system to generate reliable degradation monitoring without requiring additional sensors or excessive computational resources, as it leverages existing data infrastructure.

Inventive Principle:
Principle #25Self-service

3Measurement precision

If multiple degradation modes are accounted for, then measurement precision is improved, but device complexity and difficulty of detection increase

Engineering Contradiction:
Improvedegradation estimation precisionVSAvoidmodel structure complexity
Core Design Contradiction:
Measurement precisionVSDevice complexity

Solution Approach 1:

The model segments different degradation modes into distinct computational pathways: short-term reversible degradation (sulfur and hydrocarbon effects) and long-term irreversible degradation (thermal aging). Each segment uses a simplified temperature-dependent formulation, allowing the system to account for multiple degradation mechanisms with moderate overall complexity.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The model merges the short-term and long-term degradation estimates into a unified combined degradation estimate that the controller uses for decision-making. This merging allows the system to capture the combined effects of multiple degradation modes without requiring separate control strategies for each mode, thereby improving measurement precision while managing complexity through consolidation.

Inventive Principle:
Principle #5Merging (Combining)

4Measurement precision

If temperature-dependent degradation modeling is used, then measurement precision is improved, but use of energy for real-time calculations increases

Engineering Contradiction:
Improvedegradation monitoring precisionVSAvoidreal-time calculation energy
Core Design Contradiction:
Measurement precisionVSUse of energy by moving object

Solution Approach 1:

The model uses SCR catalyst temperature, a parameter that is already measured and available in real-time for other aftertreatment control functions. By leveraging this existing measurement, the system achieves temperature-dependent degradation modeling without requiring additional sensors or excessive computational energy, as the temperature data serves multiple control purposes simultaneously.

Inventive Principle:
Principle #25Self-service

Data Source

PatentUS11635011B2Controller and method for controlling operation of an aftertreatment system based on short-term and long-term cumulative degradation estimates
Publication Date: 2023.04.25 CUMMINS EMISSION SOLUTIONS INC
  • US11635011B2 patent drawing
  • US11635011B2 patent drawing
  • US11635011B2 patent drawing

AI summary

A controller for controlling operation of an aftertreatment system that is configured to treat constituents of an exhaust gas produced by an engine, the aftertreatment system including a selective catalytic reduction (SCR) catalyst, the controller configured to: generate a short-term cumulative degradation estimate of the SCR catalyst corresponding to reversible degradation of the SCR catalyst due to sulfur and/or hydrocarbons based on a SCR catalyst temperature parameter; generate a long-term cumulative degradation estimate of the SCR catalyst corresponding to thermal aging of the SCR catalyst based on the SCR catalyst temperature parameter; generate a combined degradation estimate of the SCR catalyst based on the short-term cumulative degradation estimate and the long-term cumulative degradation estimate; and adjust an amount of reductant and/or an amount of hydrocarbons inserted into the aftertreatment system based on the combined degradation estimate of the SCR catalyst.