Palladium Catalyst for NOx Reduction in High Water Gas Turbine Exhaust

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Solution Overview

Problem

Current hydrogen-selective catalytic reduction (H2-SCR) technologies face challenges in achieving high NOx reduction efficiency and selectivity to N2 in the exhaust of gas turbines, particularly under conditions with high water, oxygen, and sulfur content, which are prevalent in coal-based integrated gasification combined cycle (IGCC) plants.

Innovation Solution

A palladium-based catalyst supported on sulfated ZrO2-SiO2 oxides, potentially including tungsten as a promoter, is used in a monolithic form with a washcoat to enhance stability and efficiency, with specific preparation steps involving calcination and impregnation, and activation to optimize performance in the presence of high water and sulfur levels.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If Pt-based H2-SCR catalysts are used, then NOx reduction capability is provided, but selectivity towards N2 formation is low and undesirable byproducts such as N2O and NH3 are produced

Engineering Contradiction:
ImproveNOx reduction capabilityVSAvoidselectivity towards N2 formation
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the catalyst material parameter from Pt-based to Pd-based, which fundamentally alters the reaction selectivity. Palladium-based catalysts provide high selectivity towards N2 formation while minimizing undesirable byproducts like N2O and NH3, thus resolving the contradiction between NOx reduction capability and product selectivity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent employs a composite catalyst system consisting of Pd supported on sulfated ZrO2-SiO2 oxides with tungsten as a promoter. This composite structure combines the catalytic activity of Pd with the stabilizing and selective properties of sulfated zirconia-silica, achieving both high NOx reduction efficiency and high N2 selectivity simultaneously

Inventive Principle:
Principle #40Composite materials

2Productivity

If H2-SCR is used under typical conditions, then NOx reduction is achieved, but the system lacks durability and stability in presence of high water, oxygen, and sulfur concentrations

Engineering Contradiction:
ImproveNOx reduction efficiencyVSAvoiddurability and stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent modifies the catalyst composition parameters by introducing sulfated ZrO2-SiO2 support and tungsten promoter, which fundamentally changes the catalyst's resistance to deactivation. This composite structure provides exceptional stability in harsh conditions with high water (10-25%), oxygen (5-10%), and sulfur (5-10 ppm) concentrations, maintaining durability and activity over extended periods

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent converts the harmful effects of water, oxygen, and sulfur that typically deactivate catalysts into beneficial factors. The sulfated ZrO2-SiO2 support with tungsten promoter actually enhances catalyst stability and activity in the presence of these components, transforming the previously detrimental operating conditions into favorable ones for catalyst performance

Inventive Principle:
Principle #22Blessing in disguise (Convert harm into benefit)

3Productivity

If conventional SCR systems are used, then NOx control is achieved, but ammonia slip into ambient air occurs

Engineering Contradiction:
ImproveNOx controlVSAvoidammonia slip
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The patent changes the reducing agent parameter from ammonia to hydrogen, which fundamentally eliminates the ammonia slip problem. H2-SCR using Pd-based catalysts reduces NOx to N2 and H2O without producing ammonia, thus resolving the contradiction between NOx control and ammonia emission

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent replaces ammonia, which causes pollution and requires careful handling, with hydrogen as the reducing agent. Hydrogen is cleaner, safer, and eliminates the need to manage ammonia slip, providing a superior alternative that resolves the environmental and operational issues of conventional SCR systems

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

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 greater than 90% NOx reduction efficiency with high selectivity to N2, maintaining stability over extended periods and improved performance with increased water content, suitable for industrial applications in power plants.

Implementation Method 1

A palladium-based catalyst supported on sulfated ZrO2-SiO2 oxides, potentially with tungsten as a promoter, is used in a monolithic form with a washcoat to enhance stability and efficiency, allowing for high NOx reduction to N2

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

catalytic process for reduction of nitrogen oxides (NOx) in combustion exhaust by selective catalytic reduction (SCR) using hydrogen as a reducing agent

Methodology Applied
Scientific EffectSelective catalytic reduction: Catalysis

Data Source

PatentUS7718153B2Catalytic process for control of NOx emissions using hydrogen
Publication Date: 2010.05.18 SIEMENS ENERGY INC
  • US7718153B2 patent drawing
  • US7718153B2 patent drawing
  • US7718153B2 patent drawing

AI summary

A selective catalytic reduction process with a palladium catalyst for reducing NOx in a gas, using hydrogen as a reducing agent. A zirconium sulfate (ZrO2)SO4 catalyst support material with about 0.01-2.0 wt. % Pd is applied to a catalytic bed positioned in a flow of exhaust gas at about 70-200° C. The support material may be (ZrO2—SiO2)SO4. H2O and hydrogen may be injected into the exhaust gas upstream of the catalyst to a concentration of about 15-23 vol. % H2O and a molar ratio for H2/NOx in the range of 10-100. A hydrogen-containing fuel may be synthesized in an Integrated Gasification Combined Cycle power plant for combustion in a gas turbine to produce the exhaust gas flow. A portion of the fuel may be diverted for the hydrogen injection.