PdO/Co3O4 Catalyst Direct NOx Decomposition

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Current catalysts for removing nitrogen oxides (NOx) from exhaust gas streams are inefficient at low temperatures and require reductants, limiting their practical application in vehicle exhaust systems.

Innovation Solution

A catalyst system comprising PdO dispersed on a Co3O4 spinel oxide support, which catalyzes the direct decomposition of NOx to N2 without the need for reductants, operating effectively at temperatures between 400° C. and 650° C. with high N2 selectivity.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional catalysts are used for direct NOx decomposition, then high temperature operation (>600°C) achieves acceptable activity, but this severely limits practical application in vehicle exhaust systems where temperatures are lower

Engineering Contradiction:
ImproveNOx decomposition activityVSAvoidoperating temperature
Core Design Contradiction:
ProductivityVSTemperature

Solution Approach 1:

The patent employs a composite catalyst system combining PdO (palladium oxide) dispersed on a Co3O4 (cobalt oxide) spinel support. This composite structure leverages the synergistic effects between the metal oxide catalyst and spinel support to achieve high NOx decomposition activity at lower temperatures (400-650°C) compared to conventional catalysts that require >600°C

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The invention changes the chemical and physical parameters of the catalyst system by using PdO/Co3O4 composite with specific surface area (10-50 m²/g) and PdO loading (1-3 wt%). These parameter optimizations enable the catalyst to maintain high activity in the 400-650°C temperature range, resolving the contradiction between activity and operating temperature

Inventive Principle:
Principle #35Parameter changes

2Temperature

If low temperature direct NOx decomposition catalysts are used (e.g., Cu-ZSM5, K/Co3O4, Na/Co3O4, CuO, Ag/Co3O4), then operation at lower temperatures is possible, but N2 product specificity and overall activity are insufficient for practical application

Engineering Contradiction:
Improveoperating temperatureVSAvoidN2 selectivity and catalytic activity
Core Design Contradiction:
TemperatureVSReliability

Solution Approach 1:

The PdO/Co3O4 spinel composite catalyst achieves superior N2 selectivity (>75% at 450°C) and catalytic activity compared to other low-temperature catalysts like Cu-ZSM5, K/Co3O4, Na/Co3O4, CuO, and Ag/Co3O4. The composite structure provides both the low operating temperature capability and the high reliability needed for practical application

Inventive Principle:
Principle #40Composite materials

Solution Approach 2:

The spinel support provides specific local chemical environments and surface properties that enhance the catalytic performance of PdO. The localized structure and composition of the composite material create active sites with optimal properties for selective N2 production at low temperatures

Inventive Principle:
Principle #3Local quality

3Productivity

If NOx traps or selective catalytic reduction (SCR) processes are used, then NOx removal is effective, but these processes are highly dependent on reductants (unburned hydrocarbons or CO), increasing fuel efficiency cost

Engineering Contradiction:
ImproveNOx removal efficiencyVSAvoidfuel efficiency cost
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

The patent extracts the dependency on reductants from the NOx removal process by implementing direct NOx decomposition. The PdO/Co3O4 catalyst enables NOx to decompose directly into N2 and O2 without requiring unburned hydrocarbons or CO as reducing agents, thereby eliminating the fuel efficiency penalty associated with NOx traps and SCR processes

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The direct decomposition mechanism allows the catalyst system to serve itself by decomposing NOx into N2 and O2 using only thermal energy from the exhaust stream, without needing external reductant supplies. This self-sufficient operation eliminates the energy loss associated with consuming reductants

Inventive Principle:
Principle #25Self-service

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 PdO/Co3O4 catalyst system achieves significant NOx conversion to N2 with high selectivity and stability, avoiding the production of undesirable N2O and NO2, and maintains activity over extended periods at low temperatures, improving fuel efficiency and reducing the need for reductants.

Implementation Method 1

The catalyst system may include a Co3O4 spinel oxide, and PdO dispersed on a surface of the Co3O4 spinel oxide. The catalyst system is configured to catalyze a decomposition of the NOx to generate N2 without the presence of a reductant.

Methodology Applied
Scientific EffectCatalysis: Catalysis

Data Source

PatentUS10143965B1Palladium oxide dispersed on spinel oxides as catalysts for direct NOx decomposition
Publication Date: 2018.12.04 TOYOTA JIDOSHA KK
  • US10143965B1 patent drawing
  • US10143965B1 patent drawing
  • US10143965B1 patent drawing

AI summary

Active catalysts for the treatment of a low temperature exhaust gas stream are provided containing palladium oxides dispersed on a spinel oxide for the direct, lean removal of nitrogen oxides from the exhaust gas stream. The low temperature (from about 400° C. to about 650° C.), direct decomposition is accomplished without the need of a reductant molecule. In one example, PdO may be dispersed on a surface of a metal oxide support, such as Co3O4 spinel oxide, synthesized using wet impregnation techniques. The PdO/Co3O4 catalyst system converts nitric oxide to nitrogen gas with high product specificity, avoiding the production of a significant concentration of the undesirable N2O product.