Diesel Oxidation Catalyst Heat Profile for Stable NO Oxidation

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Solution Overview

Problem

Existing diesel oxidation catalysts face challenges in maintaining consistent performance across their service life, particularly in stabilizing NO oxidation activity while minimizing the impact on CO/HC oxidation and exotherm generation capabilities.

Innovation Solution

A method involving a two-stage thermal treatment process is applied to a diesel oxidation catalyst, where a first heat treatment at a high temperature stabilizes the NO oxidation activity, followed by a second treatment at a lower temperature to maintain CO/HC oxidation and exotherm generation properties, with a higher platinum-group-metal concentration at the inlet end for efficient exotherm generation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a single high-temperature heat treatment is applied to stabilize NO oxidation activity, then NO oxidation performance is improved, but CO/HC oxidation and exotherm generation capabilities deteriorate

Engineering Contradiction:
ImproveNO oxidation performance stabilityVSAvoidCO/HC oxidation and exotherm generation capability
Core Design Contradiction:
ReliabilityVSProductivity

Solution Approach 1:

The heat treatment process is segmented into two distinct stages: a first heat treatment at a first maximum temperature to stabilize NO oxidation activity, and a second heat treatment at a second maximum temperature (at least 25°C lower) to preserve CO/HC oxidation and exotherm generation capabilities. This segmentation allows each treatment to optimize specific catalyst functions independently, resolving the contradiction between stabilizing NO oxidation and maintaining other catalytic activities.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention changes the temperature parameter between the two heat treatment stages, with the second maximum temperature being at least 25°C lower than the first maximum temperature. This parameter change enables differential effects on various catalytic components, stabilizing NO oxidation activity while preserving the exotherm generation capability and CO/HC oxidation performance.

Inventive Principle:
Principle #35Parameter changes

2Power

If platinum-group-metal concentration is increased at the inlet end for exotherm generation, then exotherm generation capability is improved, but manufacturing complexity increases

Engineering Contradiction:
Improveexotherm generation capabilityVSAvoidmanufacturing complexity
Core Design Contradiction:
PowerVSDevice complexity

Solution Approach 1:

The invention applies local quality by concentrating platinum-group-metals at the inlet end of the catalyst where exotherm generation is most needed, rather than uniformly distributing them throughout. This localized concentration optimizes exotherm generation capability at the critical inlet region while reducing overall manufacturing complexity compared to uniform high-concentration distribution.

Inventive Principle:
Principle #3Local quality

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

The method results in a catalyst with stabilized NO oxidation performance and maintained CO/HC oxidation and exotherm generation capabilities, reducing the performance delta over the catalyst's lifetime and optimizing the NO2/NO ratio for downstream components like SCR catalysts.

Implementation Method 1

subjecting the first coated substrate to a first heat treatment to form a heat-treated coated substrate, wherein the first heat treatment comprises heating the first coated substrate to a first maximum temperature and holding the first coated substrate at the first maximum temperature

Methodology Applied
Scientific EffectHeat treatment: Heat Treatment

Implementation Method 2

This catalyst converts particulate matter (PM), hydrocarbons, and carbon monoxide to carbon dioxide and water

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

The DOC can also be used to promote the conversion of NO to NO2 for downstream passive filter regeneration

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 4

subjecting the second coated substrate to a second heat treatment to form the diesel oxidation catalyst, wherein the second heat treatment comprises heating the second coated substrate to a second maximum temperature and holding the second coated substrate at the second maximum temperature

Methodology Applied
Scientific EffectHeat treatment: Heat Treatment

Data Source

PatentUS20250360499A1A diesel oxidation catalyst and a method for its manufacture
Publication Date: 2025.11.27 JOHNSON MATTHEY PLC
  • US20250360499A1 patent drawing
  • US20250360499A1 patent drawing
  • US20250360499A1 patent drawing

AI summary

A method for the manufacture of a diesel oxidation catalyst comprises: (i) providing a carrier substrate; (ii) forming one or more platinum-group-metal-containing washcoat layers each comprising a refractory metal oxide support material on the carrier substrate to provide a first coated substrate; (iii) subjecting the first coated substrate to a first heat treatment to form a heat-treated coated substrate, wherein the first heat treatment comprises heating the first coated substrate to a first maximum temperature and holding the first coated substrate at the first maximum temperature; (iv) depositing a platinum-group-metal-containing composition comprising a refractory metal oxide support material on at least a portion of the heat-treated coated substrate to form a second coated substrate; and (v) subjecting the second coated substrate to a second heat treatment to form the diesel oxidation catalyst, wherein the second heat treatment comprises heating the second coated substrate to a second maximum temperature and holding the second coated substrate at the second maximum temperature; wherein the first maximum temperature is at least 600° C. and wherein the second maximum temperature is at least 25° C. lower than the first maximum temperature.