High-Temperature Three-Way Catalyst Chamber for Biomass NOx Control

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Solution Overview

Problem

Conventional biomass combustion technologies produce high nitrogen oxide emissions, requiring costly secondary measures like SNCR and SCR systems, which are complex and inefficient, and three-way catalytic converters are not effectively used due to the inhomogeneity of biomass fuels, making NOx reduction challenging.

Innovation Solution

Integrate a high-temperature three-way catalyst into the gas combustion chamber with staged air supply and temperature control to achieve near-stoichiometric operation, combining partial and superstoichiometric combustion zones to catalytically reduce NOx, CO, and hydrocarbons efficiently.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Temperature

If conventional biomass combustion technologies are used, then hot flue gases can be generated for steam and hot water production, but high nitrogen oxide emissions are released

Engineering Contradiction:
Improveflue gas temperatureVSAvoidnitrogen oxide emissions
Core Design Contradiction:
TemperatureVSObject-generated harmful factors

Solution Approach 1:

The combustion chamber is segmented into multiple zones with different oxygen concentrations. The first combustion zone operates with limited oxygen (substoichiometric) to prevent excessive NOx formation, while the second zone provides sufficient oxygen (superstoichiometric) for complete combustion. This spatial segmentation allows simultaneous control of NOx emissions and combustion efficiency.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention changes the oxygen concentration parameter along the combustion path. By controlling the air-to-fuel ratio to first be below stoichiometric (λ < 1) and then above stoichiometric (λ > 1), the system optimizes both NOx reduction and combustion completeness. The three-way catalyst further utilizes this parameter change to achieve efficient conversion.

Inventive Principle:
Principle #35Parameter changes

2Object-generated harmful factors

If staged combustion systems are used to reduce NOx emissions, then nitrogen oxide emissions are somewhat reduced, but the reduction is insufficient to meet stringent NOx limits

Engineering Contradiction:
Improvenitrogen oxide emissionsVSAvoidNOx emission control effectiveness
Core Design Contradiction:
Object-generated harmful factorsVSReliability

Solution Approach 1:

A three-way catalyst is introduced as an intermediary component between the two combustion zones. This catalyst mediates the chemical reactions to achieve simultaneous reduction of NOx, CO, and hydrocarbons. The catalyst enables the system to meet stringent NOx limits by facilitating efficient conversion reactions that staged combustion alone cannot achieve.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The three-way catalyst employs composite material structure combining different metallic components (such as Pt, Pd, Rh) supported on ceramic substrates with specific washcoats. This composite structure provides multiple active sites for simultaneous oxidation and reduction reactions, ensuring reliable NOx emission control below 50 mg/Nm³.

Inventive Principle:
Principle #40Composite materials

3Object-generated harmful factors

If SNCR or SCR systems are used for exhaust gas aftertreatment, then NOx emissions are further reduced, but investment and operating expenses increase significantly

Engineering Contradiction:
Improvenitrogen oxide emissionsVSAvoidsystem complexity
Core Design Contradiction:
Object-generated harmful factorsVSDevice complexity

Solution Approach 1:

The invention merges the combustion process with the catalytic aftertreatment process by integrating the three-way catalyst directly into the combustion chamber. This combination eliminates the need for separate SNCR or SCR systems, reducing both investment costs and operational complexity while achieving comparable or superior NOx reduction performance.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The three-way catalyst performs multiple functions simultaneously: it reduces NOx emissions, oxidizes CO to CO2, and oxidizes unburned hydrocarbons. This multi-functionality replaces the need for separate treatment systems for different pollutants, simplifying the overall system while maintaining comprehensive emission control.

Inventive Principle:
Principle #6Universality (Multi-functionality)

4Object-generated harmful factors

If three-way catalytic converters are used with biomass fuels, then NOx reduction can be achieved, but the inhomogeneity of biomass fuels makes effective use difficult

Engineering Contradiction:
Improvenitrogen oxide emissionsVSAvoidoperational control
Core Design Contradiction:
Object-generated harmful factorsVSEase of operation

Solution Approach 1:

The system employs dynamic control of the air-to-fuel ratio to adapt to the inhomogeneity of biomass fuels. By continuously adjusting the oxygen supply in both combustion zones and regulating the lambda value, the system maintains optimal conditions for the three-way catalyst despite variations in fuel composition, ensuring stable NOx reduction performance.

Inventive Principle:
Principle #15Dynamics

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 method effectively reduces NOx emissions without expensive reducing agents, achieving high conversion rates and simplifying the integration of three-way catalytic converters in biomass combustion systems.

Implementation Method 1

an integrated high-temperature three-way catalyst 5, which divides the gas combustion chamber 2 into a front area 6 and a rear area 7

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

the temperature is regulated to a value between 800°C and 1000°C by cooling

Methodology Applied
Scientific EffectCooling: Cooling

Implementation Method 3

hot flue gases produced in this way can be used for several purposes, e.g. for the production of steam, hot water or hot thermal oils

Methodology Applied
Scientific EffectCombustion: Combustion

Data Source

PatentEP4459182B1Method and device for producing a flue gas
Publication Date: 2025.10.29 POLYTECHNIK LUFT UND FEUERUNGSTECHNIK GMBH
  • EP4459182B1 patent drawingFigure 1~2
  • EP4459182B1 patent drawingFigure 3~4
  • EP4459182B1 patent drawingFigure 5

AI summary

In a process for generating flue gas from a gas or gas mixture produced directly or indirectly from solid biomass fuels, the flue gas is generated in a gas combustion chamber (2) which has a gas inlet (3) at one end, a gas outlet (4) at the other end, and an integrated high-temperature three-way catalyst (5) between them. The high-temperature three-way catalyst (5) divides the gas combustion chamber (2) into a front section (6) and a rear section (7) with thermally insulated walls (8), both viewed in the direction of flow (S).The process involves the following steps performed sequentially in the direction of flow (S): • Introducing the gas into the gas combustion chamber (2), • Combusting the gas or gas mixture in a first combustion zone (11), at a combustion air ratio regulated to 0.80 to 0.99 and a temperature regulated to 800°C to 1000°C, • Cleaning the gas in the high-temperature 3-way catalyst (5), • Post-combustion of the gas in a second combustion zone (16), at a combustion air ratio regulated to &gt; 1 and a temperature of &gt; 800°C, • Expelling the generated flue gas from the gas combustion chamber.