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The Influence of Corrosion and Wear on FGD Desulfurization Unit of Desulfurization and Denitration Pump in Thermal Power Plant
The influence of corrosion and wear on the FGD desulfurization device of the desulfurization and denitration pump in thermal power plants:
Corrosion and wear parts:
Parts prone to corrosion: absorption tower, clean flue and inlet flue of absorption tower
Parts prone to wear: absorption tower, slurry pipeline, pump casing and impeller
Causes of corrosion and wear
Corrosion reasons: the presence of chloride ions and sulfate (sub) ions starts from the weak point of the anti-corrosion layer and slowly corrodes; low-temperature corrosion and electrochemical corrosion.
Reasons for wear: excessive dust and SiO 2 content
Of course, corrosion and wear are mutual. After corrosion, there is wear; after wear, there is corrosion.
Measures taken to prevent corrosion of FGD desulfurization device of desulfurization and denitration pump in thermal power plant:
Glass resin flakes for corrosion protection
Rubber lining for corrosion protection
Corrosion-resistant alloy material (C276 or 1.4529)
Non-metallic FRP material for corrosion protection

- Capacity:60-33005m³/h
- Head:0.95-30.2bar
- Price:$2200-215000

- Capacity:60-33005m³/h
- Head:0.95-30.2bar
- Price:$2200-215000

- Capacity:5.5-2600m³/h
- Head:1.6-25bar
- Price:$4300-37000

- Capacity:5.5~400m³/h
- Head:0.42-12.5bar
- Price:$560-9800