" />
Temperature capability and corrosion resistance frequently conflict: 310S resists scaling well but is attacked by chlorides, while 316L resists corrosion but loses strength as temperature rises. The approach is to fix the material route from the medium first and then support it with lining and process measures.
First establish whether the medium is oxidising or contains chlorides or sulphur, then trade off temperature capability against corrosion resistance.
| Location | Combination | Basis |
| Impeller | 316L, 310S or nickel alloy | Grade confirmed from medium and temperature |
| Casing lining | Ceramic fibre with corrosion resistant barrier | Addresses insulation and corrosion together |
| Shaft | Heat resistant alloy with thermal sleeve | Controls the shaft temperature gradient |
| Shaft seal | High temperature graphite or PTFE combination | Combines temperature capability and sealing |
| Fasteners | Heat resistant stainless steel | Prevents oxidation seizure |
| Location | Combination | Basis |
| Dew point control | Operation above the acid dew point | Avoids condensation driven corrosion |
| Heat-up curve | Controlled heating with moisture removal | Protects lining and welds |
| Expansion joints | Divided according to thermal growth | Releases thermal stress |
| Lining anchoring | Anchors fix the insulation layer | Prevents detachment blocking the flow path |
| Temperature survey | Thermocouples with periodic measurement | Finds local hot spots early |
Applications include sulphur bearing flue gas heat recovery, chloride bearing hot gas, hazardous waste incineration tail gas and metallurgical and chemical hot gas.
At the same temperature, oxidising and chloride bearing media can lead to opposite material conclusions, so temperature alone is not a sufficient basis for selection.
Start-up and shutdown are when the lining and welds are most likely to crack, so heating and cooling rates should be written into the operating procedure.
| Standard | Title | Purpose |
| HG/T 20679 | Design code for external anti-corrosion of chemical equipment and piping | Anti-corrosion design for chemical media |
| GB/T 4237 | Hot rolled stainless steel plate, sheet and strip | Stainless impeller and casing material |
| GB/T 20878 | Stainless and heat-resisting steels - Designation and chemical composition | High temperature and corrosion resistant grades |
| GB/T 3003 | Refractory fibres and products | High temperature lining material and acceptance |
| GB/T 1236 | Industrial fans - Performance testing using standardized airways | Air flow, pressure and efficiency testing |
Please provide medium composition, medium temperature and dew point, dust load and air flow. Size and motor power are calculated for the actual duty.
First determine the corrosion type from the medium: oxidising high temperature service tends towards high nickel chromium stainless steel such as 310S, while chloride bearing or reducing service requires avoiding high nickel grades and considering nickel alloys or a non-metallic lining. The answer follows the medium rather than the temperature alone.
Its weakness is chloride resistance. In chloride bearing gas or dust it is prone to pitting and stress corrosion, so a more chloride resistant material or an isolating layer is required.
Three measures together: keep the operating temperature above the acid dew point, avoid condensation during shutdowns, and select materials for wet conditions rather than dry conditions. Missing any one of the three shortens service life.
Related pages: Non-standard fan range high temperature fan range Anti-corrosion fan range
Contact: Lee
Phone: 13793313126
Tel: 0533-6820280
Email: chuanyi99@126.com
Add: Wujia Industrial Park, Nanjiao Town, Zhoucun District, Zibo City, Shandong Province, China