Wall-Flow Filter with Dual Coatings for Back Pressure Management

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Solution Overview

Problem

Current particulate filters face a trade-off between catalytic activity and filtration efficiency, often resulting in increased exhaust-gas back pressure, which limits their effectiveness in reducing harmful emissions from internal combustion engines.

Innovation Solution

A wall-flow filter design featuring a catalytically active coating (Z) in the porous walls and a membrane coating (F) on the surfaces, with palladium and/or rhodium, and a cerium/zirconium mixed oxide, optimized to balance catalytic activity and filtration efficiency while minimizing back pressure.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If a catalytically active coating is applied to the channel walls of a wall-flow filter, then catalytic effectiveness is improved, but exhaust-gas back pressure increases

Engineering Contradiction:
Improvecatalytic effectivenessVSAvoidexhaust-gas back pressure
Core Design Contradiction:
ReliabilityVSStress or pressure

Solution Approach 1:

The patent applies different coatings to different locations: coating Z (catalytically active with Pd/Rh and cerium/zirconium mixed oxide) is applied to the porous walls and/or outlet channel surfaces, while coating F (filtration membrane without noble metal) is applied mainly to inlet channel surfaces. This local differentiation optimizes catalytic activity where needed while minimizing back pressure increase at the inlet.

Inventive Principle:
Principle #3Local quality

2Stress or pressure

If the amount of oxidic support materials for catalytic noble metals is reduced in a filter, then exhaust-gas back pressure is minimized, but catalytic effectiveness deteriorates

Engineering Contradiction:
Improveexhaust-gas back pressureVSAvoidcatalytic effectiveness
Core Design Contradiction:
Stress or pressureVSReliability

Solution Approach 1:

The patent uses a composite coating system combining coating Z (containing Pd/Rh noble metals with cerium/zirconium mixed oxide support) and coating F (filtration membrane without noble metal). This composite approach provides catalytic functionality with reduced oxidic support material quantities while maintaining effectiveness.

Inventive Principle:
Principle #40Composite materials

3Stress or pressure

If catalytically active material is dispersed in the porous walls (in-wall coating), then exhaust-gas back pressure is reduced, but the amount of catalytic substance is limited by absorption capacity

Engineering Contradiction:
Improveexhaust-gas back pressureVSAvoidamount of catalytic substance
Core Design Contradiction:
Stress or pressureVSQuantity of substance

Solution Approach 1:

The patent transitions from purely in-wall coating to on-wall coating by applying coating Z to the surfaces of the channel walls (particularly outlet channels) and coating F to inlet channel surfaces. This surface-based approach provides additional dimension for catalytic material placement beyond pore absorption, increasing the quantity of catalytic substance while maintaining low back pressure.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

4Reliability

If a filtration layer is created on inlet channel walls, then filtration efficiency is improved, but device complexity increases

Engineering Contradiction:
Improvefiltration efficiencyVSAvoidcoating structure complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The patent merges filtration and catalysis functions into a single integrated coating system. Coating F provides filtration membrane functionality on inlet surfaces, while coating Z provides catalytic activity on outlet surfaces and porous walls. This merging eliminates the need for separate filtration and catalysis components, reducing overall device complexity.

Inventive Principle:
Principle #5Merging (Combining)

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 filter achieves enhanced filtration efficiency and catalytic activity with a moderate increase in exhaust-gas back pressure, improving soot particle deposition and burn-off, and maintaining stability even when exposed to condensation water.

Implementation Method 1

The catalytically active coating Z... comprises palladium and/or rhodium and a cerium/zirconium mixed oxide

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

The wall-flow filter substrate has... coatings Z and F that differ from one another... the coating F is located mainly on the surfaces OE

Methodology Applied
Scientific EffectFiltration: Filter (physical)

Implementation Method 3

the wall-flow filter substrate has channels E and A, which extend in parallel between a first and a second end of the wall-flow filter substrate, are separated by porous walls

Methodology Applied
Scientific EffectPorosity: Porosity

Data Source

PatentUS20240033687A1Catalytically active particle filter with a high degree of filtering efficiency
Publication Date: 2024.02.01 UMICORE AG & CO KG
  • US20240033687A1 patent drawing
  • US20240033687A1 patent drawing
  • US20240033687A1 patent drawing

AI summary

The invention relates to a wall flow filter for removing particulate matter from the exhaust of internal combustion engines, comprising a wall flow filter substrate having a length L, and different coatings Z and F, the wall flow filter substrate being provided with channels E and A which run parallel between a first end and a second end of the wall flow filter substrate, are separated by porous walls, and form surfaces OE and OA, respectively; channels E are closed at the second end, and channels A are closed at the first end; coating Z is disposed in the porous walls and/or on surfaces OA, but not on surfaces OE, and contains palladium and/or rhodium and a cerium/zirconium mixed oxide; coating F is disposed mainly on surfaces OE, but not on surfaces OA, and comprises a membrane and no precious metal. The wall flow filter is characterized in that the mass ratio of coating Z to coating F ranges from 0.1 to 25.