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Mechanisms, Hazards, and Prevention Strategies for Alkali Metal Poisoning in SCR DeNOx Catalysts


Release time:

Apr 24,2026

Selective Catalytic Reduction (SCR) is the mainstream technology for controlling nitrogen oxides in coal-fired power plants, biomass boilers, and industrial furnaces. Alkali metal (Na, K) poisoning is one of the key factors leading to irreversible catalyst deactivation and a significant reduction in catalyst lifespan.

Selective Catalytic Reduction (SCR) is the mainstream technology for controlling nitrogen oxides in coal-fired power plants, biomass boilers, and industrial furnaces. Alkali metal (Na, K) poisoning is one of the key factors leading to irreversible catalyst deactivation and a significant reduction in catalyst lifespan.
Water-soluble sodium and potassium salts in flue gas can penetrate deep into the catalyst’s pores, destroying acidic active sites through a dual mechanism of chemical poisoning and physical blockage. This significantly reduces DeNOx efficiency and increases operational and maintenance costs as well as environmental emission risks. This paper systematically discusses the sources of alkali metals, their mechanisms of action, their impact on performance, and end-to-end prevention and control technologies, providing a technical reference for the stable operation of catalysts under high-alkali-metal conditions.
I. Sources, Migration, and Transformation of Alkali Metals
Coal and biomass fuels commonly contain alkali metal elements such as sodium (Na), potassium (K), and arsenic (As), which, after combustion, enter the SCR system with flue gas in the form of gaseous oxides, chlorides, sulfates, and other compounds.
● In coal, alkali metals are primarily found in minerals such as feldspar and mica, and are released as water-soluble components at high temperatures;
● Flue gas from biomass fuels and waste incineration contains higher levels of water-soluble K⁺ and Na⁺, resulting in a significantly higher risk of catalyst poisoning compared to pure coal combustion;
● Alkali metal salts have small particle sizes and are highly mobile; they can enter the catalyst bed with the flue gas and, upon condensation with water vapor, accelerate their penetration into the internal pores.
II. Mechanisms of Alkali Metal Poisoning in DeNOx Catalysts
1. Chemical Poisoning (Irreversible Deactivation of the Core)
Alkali metals (represented by K₂O and Na₂O) are strongly basic and preferentially undergo neutralization reactions with Brønsted acid sites (V–OH) on the catalyst surface, forming inactive salts such as V–OK and V–ONa.
● Directly occupy acidic sites, blocking NH₃ adsorption and activation, and inhibiting the formation of the active NH₄⁺ intermediate;
● Disrupt the electronic structure of V₂O₅–WO₃(MoO₃)/TiO₂, reducing redox capacity and catalytic cycle efficiency;
● Studies indicate that when the K₂O loading exceeds 1%, the catalyst can be completely deactivated, and full recovery through conventional regeneration is difficult.
2. Physical Blockage and Coating
Alkali metal salts deposit and agglomerate at pore entrances and within pores, forming a dense coating layer:
● Reducing specific surface area, pore volume, and porosity, thereby hindering NO and NH₃ diffusion and mass transfer;
● Agglomerating with fly ash and ammonium sulfate salts, increasing reactor resistance, and exacerbating localized ash blockage and gas flow deviation.
3. Structural Degradation
Alkali metal intrusion weakens the crystalline stability of the TiO₂ support, leading to the following issues during long-term operation:
● Agglomeration of support particles and sintering of micropores;
● Decreased mechanical strength, increasing the risk of wear, collapse, and fracture, and shortening the replacement cycle.
III. The Adverse Effects of Alkali Metal Poisoning on Catalyst Performance
● Rapid decline in DeNOx efficiency: Even the continuous accumulation of trace amounts of alkali metals can lead to a decline in activity; under high-alkali conditions, efficiency drops significantly within a few months;
● Drastically shortened active life: Lifespan is reduced by 30%–60% compared to normal operating conditions, with biomass boilers being particularly affected;
● Significant increase in ammonia slip: Excessive ammonia injection to maintain efficiency leads to air preheater blockages, corrosion, and increased fan energy consumption;
● Soaring operating costs: Shorter replacement cycles and increased regeneration difficulty result in a substantial rise in O&M expenses;
● Increased risk of emission non-compliance: Difficulty in consistently meeting ultra-low NOₓ emission requirements creates a risk of environmental penalties.
IV. Methods for Diagnosing and Characterizing Alkali Metal Poisoning
1. Elemental Analysis
Determine Na and K content via XRF and ICP–MS; a K₂O + Na₂O content exceeding 1% is considered indicative of significant poisoning.
2. Structural Analysis
● BET: Significant deterioration in specific surface area, pore volume, and pore size distribution;
● XRD: Detection of inert phases such as potassium/sodium vanadate salts; changes in the carrier crystal phase.
3. Activity Evaluation
NH₃–TPD and H₂–TPR analyses show a simultaneous decrease in surface acidity and reducing capacity, with restricted reaction kinetics.
4. On-Site Operational Characterization
Decreased DeNOx efficiency, increased ammonia slip, abnormal rise in reactor pressure differential, and sustained increase in ammonia injection rate.
V. Alkali Metal Poisoning Prevention, Control, and Treatment Technologies
1. Source Control of Alkali Metals (Most Economical and Effective)
● Fuel Management: Select coal types with low alkali metal content and blend biomass with coal in appropriate proportions to reduce the alkali content entering the furnace;
2. Upstream Flue Gas Dealkalization
Install an alkali metal treatment unit upstream of the SCR system and use a high-temperature dust removal device to remove alkali metal salts, thereby achieving upstream removal and protecting the downstream catalyst.
3. Alkali-Resistant Catalyst Design
● Structural Optimization: Select carriers with large pore diameters, high porosity, and thick walls to enhance resistance to clogging and permeation;
● Formulation Modification: Increase the proportion of WO₃ and MoO₃ additives to prioritize binding with alkali metals and protect V–OH active sites;
● Surface Modification: Introduce acidic coatings to inhibit the adsorption, migration, and diffusion of alkali metals.
4. Operational Optimization and Regeneration
● Strict Temperature Control: Maintain the optimal reaction range of 300–380°C to prevent low-temperature water vapor condensation and the dissolution and migration of alkali metal salts;
● Enhanced Soot Blowing: Reasonably increase the frequency and pressure of soot blowing to reduce deposits at orifices and prevent caking;
● Tiered Replacement: Since the upper layer of catalyst is prone to poisoning first, conduct periodic sampling and replacement to reduce overall operational and maintenance costs;
● Regeneration Strategy: For mild poisoning, acid washing can remove alkali and restore activity; for severe poisoning, where chemical bonds are strong, regeneration effectiveness is limited, so direct replacement is recommended.
VI. Conclusion
Alkali metal poisoning is an irreversible deactivation caused primarily by chemical poisoning and secondarily by physical blockage; it is the primary failure mode of SCR systems under coal/biomass co-firing and high-alkali fuel operating conditions.
Prevention and control must adhere to a comprehensive four-pronged approach: source-level alkali control, upstream alkali removal, alkali-resistant catalyst selection, and optimized operation. By precisely monitoring alkali metal content and employing alkali-resistant catalysts and upstream alkali removal technologies, it is possible to effectively slow the poisoning process, extend catalyst lifespan, and ensure long-term, stable compliance with emission standards for the DeNOx system.

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