Aftertreatment Catalyst Desulfation via Staged Temperature Control

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Solution Overview

Problem

Conventional aftertreatment systems for internal combustion engines face challenges in efficiently desulfating oxidation and SCR catalysts when exposed to high sulfur content fuels, leading to rapid hydrothermal aging and reduced NOX conversion efficiency, as high regeneration temperatures used for sulfur removal also accelerate catalyst deterioration.

Innovation Solution

The system heats the oxidation and SCR catalysts to a lower regeneration temperature (400-550°C) for desulfation, reducing hydrothermal aging and maintaining catalyst efficiency, while also adjusting temperatures based on NOX conversion efficiency and sulfur concentration to prevent thermal damage and extend catalyst life.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If high regeneration temperature is used for sulfur removal, then desulfation efficiency is improved, but hydrothermal aging accelerates and catalyst life decreases

Engineering Contradiction:
Improvedesulfation efficiencyVSAvoidcatalyst life
Core Design Contradiction:
ProductivityVSDuration of action of stationary object

Solution Approach 1:

The system implements periodic regeneration cycles where the catalyst is heated to elevated temperatures (e.g., 650-850°C) for controlled durations to remove sulfur deposits. This periodic action allows efficient desulfation while limiting cumulative thermal exposure that causes hydrothermal aging, thereby extending catalyst life compared to continuous high-temperature operation.

Inventive Principle:
Principle #19Periodic action

Solution Approach 2:

The system dynamically adjusts regeneration temperature parameters based on catalyst sulfur loading levels and age. By optimizing the temperature-time profile (e.g., using lower temperatures for shorter periods or staged heating), the system achieves effective desulfation while minimizing hydrothermal aging effects that would otherwise rapidly degrade catalyst performance.

Inventive Principle:
Principle #35Parameter changes

2Loss of substance

If high regeneration temperature is used for sulfur removal, then sulfur accumulation is reduced, but NOX conversion efficiency deteriorates

Engineering Contradiction:
Improvesulfur accumulationVSAvoidNOX conversion efficiency
Core Design Contradiction:
Loss of substanceVSReliability

Solution Approach 1:

The system performs periodic regeneration to remove sulfur deposits that would otherwise poison the SCR catalyst and reduce NOX conversion efficiency. By scheduling regeneration at optimal intervals based on sulfur accumulation monitoring, the system maintains high NOX conversion efficiency while effectively managing sulfur levels.

Inventive Principle:
Principle #19Periodic action

Solution Approach 2:

The system monitors NOX conversion efficiency and sulfur accumulation levels to trigger regeneration events. When sensors detect declining NOX conversion efficiency indicative of sulfur poisoning, the system initiates targeted regeneration to restore catalyst performance, thereby maintaining reliable NOX emission control.

Inventive Principle:
Principle #23Feedback

3Loss of substance

If conventional regeneration temperature is used, then sulfur is removed from catalyst, but thermal damage increases and catalyst deterioration accelerates

Engineering Contradiction:
Improvesulfur removalVSAvoidthermal damage
Core Design Contradiction:
Loss of substanceVSObject-affected harmful factors

Solution Approach 1:

The system optimizes the temperature parameter for regeneration by using the minimum necessary temperature to achieve effective sulfur removal. Rather than consistently applying high temperatures, the system adjusts the temperature profile based on actual sulfur loading, thereby achieving sulfur removal while minimizing thermal damage and catalyst deterioration.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The system applies partial regeneration action by heating only the catalyst portion containing sulfur deposits to regeneration temperature, rather than heating the entire exhaust system. This localized or selective heating approach achieves sulfur removal while reducing overall thermal exposure and associated damage.

Inventive Principle:
Principle #16Partial or excessive action

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach effectively desulfates catalysts, prevents thermal aging, allows operation with high sulfur fuels, and increases catalyst life, reducing maintenance and warranty costs by limiting the need for overdesigning the aftertreatment system.

Implementation Method 1

certain exhaust gas aftertreatment systems for diesel-powered IC engines comprise an oxidation catalyst for oxidizing carbon monoxide (CO) or unburnt hydrocarbons

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 2

Aftertreatment systems may also include a selective catalytic reduction (SCR) system for decomposing constituents of the exhaust gas such as nitric oxides (NOX) gases

Methodology Applied
Scientific EffectSelective catalytic reduction: Catalysis

Implementation Method 3

heating an oxidation catalyst or a SCR catalyst to a regeneration temperature lower than a conventional regeneration temperature so as to desulfate the oxidation catalyst or the SCR catalyst

Methodology Applied
Scientific EffectThermal heating: Heating

Data Source

PatentUS11867106B2Systems and methods for desulfation of catalysts included in aftertreatment systems
Publication Date: 2024.01.09 CUMMINS EMISSION SOLUTIONS INC
  • US11867106B2 patent drawing
  • US11867106B2 patent drawing
  • US11867106B2 patent drawing

AI summary

An aftertreatment system for reducing constituents of an exhaust gas having a sulfur content includes: an oxidation catalyst; a filter disposed downstream of the oxidation catalyst; and a controller configured to, in response to determining that the filter is to be regenerated and a desulfation condition being satisfied: cause a temperature of the oxidation catalyst to increase to a first regeneration temperature that is greater than or equal to 400 degrees Celsius and less than 550 degrees Celsius, cause the temperature of the oxidation catalyst to be maintained at the first regeneration temperature for a first time period, and after the first time period, cause the temperature of the oxidation catalyst to increase to a second regeneration temperature equal to or greater than 550 degrees Celsius.