Low Temperature Hydrocarbon SCR Catalyst

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current selective catalytic reduction (SCR) technologies for NOx in combustion exhaust gases are limited by low activity at temperatures below 150°C, particularly during the cold start of lean-burn internal combustion engines, where existing catalysts are not active until the temperature rises sufficiently, leading to increased NOx emissions.

Innovation Solution

A method involving a transition metal/zeolite catalyst system that oxidizes nitrogen monoxide (NO) to nitrogen dioxide (NO2) at catalyst bed temperatures below 50°C and reduces NOx using a hydrocarbon reductant at temperatures below 150°C, with the hydrocarbon reductant either adsorbed on the catalyst or present in the exhaust gas, promoting NOx conversion to nitrogen (N2).

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If conventional SCR catalysts are used, then NOx reduction is achieved at high temperatures (350-500°C), but NOx emissions increase during cold start periods when temperature is below 150°C

Engineering Contradiction:
ImproveNOx reduction effectivenessVSAvoidNOx emissions during cold start
Core Design Contradiction:
ReliabilityVSObject-affected harmful factors

Solution Approach 1:

The patent changes the chemical composition parameters of the catalyst by incorporating specific metal complexes (copper, iron, or manganese) coordinated with nitrogen-containing ligands (terpyridine, bipyridine, phenanthroline) on zeolite supports. This compositional modification enables the catalyst to achieve NOx reduction activity at temperatures below 150°C, directly resolving the cold start emission problem while maintaining reliability across the full temperature range.

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The invention creates a composite catalyst system combining zeolite support materials (such as ZSM-5, beta-zeolite, or Y-zeolite) with metal complexes featuring specific coordination chemistry. This composite structure integrates the high surface area and acidity of zeolites with the redox activity of metal-nitrogen complexes, enabling effective NOx reduction at low temperatures while preserving catalyst stability and activity at higher operating temperatures.

Inventive Principle:
Principle #40Composite materials

2Reliability

If hydrocarbon reductant is used for SCR, then NOx conversion to N2 is achieved, but competitive non-selective reaction with oxygen occurs in high oxygen content exhaust gases

Engineering Contradiction:
ImproveNOx conversion efficiencyVSAvoidNon-selective hydrocarbon oxidation
Core Design Contradiction:
ReliabilityVSObject-generated harmful factors

Solution Approach 1:

The metal-nitrogen complex acts as an intermediary that facilitates selective NOx reduction by providing a specific reaction pathway. The coordinated nitrogen ligands create active sites that preferentially interact with NOx molecules through coordination chemistry, enabling the hydrocarbon reductant to react with NOx rather than oxygen, thus suppressing non-selective oxidation even in high oxygen environments.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent modifies the reaction selectivity by changing the catalyst's chemical environment through metal coordination chemistry. The specific ligand field created by nitrogen-containing ligands alters the electronic properties of the metal center, making it more selective toward NOx activation. This parameter change in the catalyst's chemical state enables preferential NOx reduction over hydrocarbon oxidation.

Inventive Principle:
Principle #35Parameter changes

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 enables significant NOx reduction at low temperatures, effectively addressing the challenge of high NOx emissions during cold starts by achieving NOx conversion rates not previously possible with existing SCR technologies.

Implementation Method 1

oxidizing nitrogen monoxide (NO) to nitrogen dioxide (NO2) on a transition metal/zeolite catalyst at catalyst bed temperatures below 50° C.

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

oxidizing nitrogen monoxide (NO) to nitrogen dioxide (NO2)

Methodology Applied
Scientific EffectOxidation: Oxidation

Implementation Method 3

reducing NOx with the catalyst using an hydrocarbon (HC) reductant at catalyst bed temperatures below 150° C.

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 4

reducing nitrogen oxides (NOx) in a flowing combustion exhaust gas to N2

Methodology Applied
Scientific EffectReduction: Reduction

Implementation Method 5

with the hydrocarbon reductant either adsorbed on the catalyst or present in the exhaust gas

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS8715602B2Low temperature hydrocarbon SCR
Publication Date: 2014.05.06 JOHNSON MATTHEY PLC
  • US8715602B2 patent drawing
  • US8715602B2 patent drawing
  • US8715602B2 patent drawing

AI summary

A method of reducing nitrogen oxides (NOx) in a flowing combustion exhaust gas to N2, which method comprising oxidizing nitrogen monoxide to nitrogen dioxide on a transition metal/elite catalyst at catalyst bed temperatures below 50° C. and reducing NOx with the catalyst using an hydrocarbon (HC) reductant at catalyst bed temperatures below 150° C.