Multifunctional Catalyst for SCR and Hydrocarbon Oxidation

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Solution Overview

Problem

Current selective catalytic reduction (SCR) catalysts in close-coupled positions face challenges with sulfur resistance and high NOx conversion over their lifecycle, particularly due to irreversible deactivation from accidental hydrocarbon exotherms, which limits their effectiveness in Heavy-Duty Diesel systems needing to meet Euro VI and VII emissions standards.

Innovation Solution

A multifunctional catalyst is developed, comprising a flow-through substrate coated with a platinum group metal component supported on zirconia, combined with a mixed oxide of vanadium and iron supported on titania, which enhances hydrocarbon oxidation and NOx reduction while maintaining sulfur tolerance.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Speed

If SCR catalysts are positioned in close-coupled location upstream of the filter, then warm-up speed and transient NOx conversion are improved, but sulfur resistance and long-term stability deteriorate due to irreversible deactivation from hydrocarbon exotherms

Engineering Contradiction:
Improvewarm-up speedVSAvoidsulfur resistance
Core Design Contradiction:
SpeedVSReliability

Solution Approach 1:

The catalyst uses a composite material structure combining vanadia (active component) supported on titania (carrier material) with an alumina washcoat layer. This composite structure provides both high catalytic activity for fast warm-up and excellent sulfur resistance through the synergistic combination of materials, resolving the contradiction between speed of warm-up and long-term reliability in close-coupled position

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The patent optimizes specific parameters including vanadia loading (3-15 wt%), titania surface area (10-50 m²/g), and calcination temperature (400-600°C) to achieve the desired balance between rapid light-off and sulfur resistance. By controlling these parameters, the catalyst maintains high activity while resisting deactivation from hydrocarbon exotherms and sulfur exposure

Inventive Principle:
Principle #35Parameter changes

2Reliability

If vanadium-based SCR catalysts are used for sulfur tolerance, then sulfur resistance is improved, but catalyst stability under high temperature hydrocarbon exotherm conditions deteriorates due to irreversible deactivation

Engineering Contradiction:
Improvesulfur toleranceVSAvoidcatalyst stability
Core Design Contradiction:
ReliabilityVSStability of the object's composition

Solution Approach 1:

The vanadia-titania composite catalyst system provides inherent sulfur tolerance while the controlled porosity and surface properties of titania prevent irreversible deactivation under hydrocarbon exotherm conditions. The composite structure maintains compositional stability by distributing vanadia species uniformly on the titania surface, preventing aggregation and sintering at elevated temperatures

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The titania carrier material possesses controlled porosity with specific surface area (10-50 m²/g) and pore size distribution that facilitates reactant access while providing thermal stability. The porous structure allows for efficient mass transport and heat dissipation, preventing hot spots that could lead to irreversible deactivation during hydrocarbon exotherms while maintaining sulfur tolerance

Inventive Principle:
Principle #31Porous materials

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 catalyst achieves improved catalytic performance for hydrocarbon oxidation and NOx reduction, reduces nitrous oxide emissions, and maintains stability and sulfur resistance, effectively meeting stringent emissions requirements.

Implementation Method 1

a platinum group metal component supported on a first oxidic material

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

for the oxidation of hydrocarbon

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

a mixed oxide of vanadium and one or more of iron, erbium, bismuth, cerium, europium, gadolinium, holmium, lanthanum, lutetium, neodymium, praseodymium, promethium, samarium, scandium, terbium, thulium, ytterbium, yttrium, molybdenum, tungsten, manganese, cobalt, nickel, copper, aluminum and antimony

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 4

for the selective catalytic reduction of nitrogen oxides

Methodology Applied
Scientific EffectSelective catalytic reduction: Catalysis

Implementation Method 5

a platinum group metal component supported on a first oxidic material and further comprises a mixed oxide of vanadium... wherein the mixed oxide is supported on a second oxidic material

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS12257573B2Multifunctional catalyst for hydrocarbon oxidation and selective catalytic reduction of NOx
Publication Date: 2025.03.25 BASF MOBILE EMISSIONS CATALYSTS LLC
  • US12257573B2 patent drawing
  • US12257573B2 patent drawing
  • US12257573B2 patent drawing

AI summary

The present invention relates to a catalyst for the oxidation of hydrocarbon and the selective catalytic reduction of nitrogen oxides, the catalyst comprising a substrate comprising an inlet end, an outlet end, a substrate axial length extending from the inlet end to the outlet end and a plurality of passages defined by internal walls of the substrate extending therethrough; and a coating disposed on the surface of the internal walls of the substrate, wherein the surface de-fines the interface between the passages and the internal walls, wherein the coating comprises a platinum group metal component supported on a first oxidic material and further comprises a mixed oxide of vanadium and one or more of iron, erbium, bismuth, cerium, europium, gadolinium, holmium, lanthanum, lutetium, neodymium, praseodymium, promethium, samarium, scandium, terbium, thulium, ytterbium, yttrium, molybdenum, tungsten, manganese, cobalt, nickel, copper, aluminum and antimony, wherein the mixed oxide is supported on a second oxidic material.