Sulphidation Resistance of Stainless Steel
For practical consideration, sulphidation in relation to high temperature attack of stainless steel, is more a consideration of the effects of sulphur containing atmospheres, rather than a specific attack mechanism. Both oxides and sulphides may be formed depending on the atmosphere, but generally the resistance to sulphur containing gasses is related to chromium content, in the same way as oxidation.
The combustion of high sulphur level fuel oils is not normally considered hazardous to stainless steel, provided there is sufficient oxygen present to make conditions sufficiently oxidising.
Affect of sulphur containing gas conditions-sulphur dioxide
Dry sulphur dioxide is normally not considered a hazard to stainless steel, although the scaling rates are higher for a given temperature than in dry air. Damp sulphur dioxide is more aggressive, which may be similar to the comparison of dry and damp air oxidation. Higher levels of chromium are beneficial in resisting attack. Although there may be little difference between grades like 1.4301 (304), 1.4401 (316) and 1.4845 (310) at around 700°C in damp sulphur dioxide, these conditions can be expected to compromise the resistance of 1.4301 (304) at 850°C. Generally grades 1.4016 (430), 1.4301(304) and 1.4541 (321) can be considered up to 800°C in sulphur dioxide. Ferritic 1.4749 (446) and austenitic 1.4845 (310) heat resisting grades can be considered up to 1025°C and 1050°C, respectively.
Affect of sulphur containing gas conditions-hydrogen and hydrogen sulphide
Stainless steel with less than 20% chromium may form less stable chromium sulphide 'scales'. The 1.4845(310) grade (24-26% Cr in BS EN 10095) can be considered for hydrogen sulphide environments.
Combustion atmospheres with sulphur
The sulphur levels in fuels such as natural gas are low and so the combustion products of these fuels are not a hazard to stainless steel, from the point of view of sulphur content. High sulphur oil combustion products may be a hazard and it is not sensible to generalize on these.
Liquid sulphur and sulphur vapour
Liquid sulphur at up to 240°C should not attack stainless steels, but at its boiling point (445°C), liquid sulphur is very aggressive to 1.4301 (304) type. Grades such as 1.4401(316) have some resistance and may be useful under certain conditions. Sulphur vapour is very aggressive to stainless steel but the higher chromium 1.4845(310) grade may be worth considering.
Sulfuric Acid Corrosion H2SO4 Corrosion
Sulphidation Resistance of Stainless Steel
Selection of Stainless Steel fo Handling Sulphur Dioxide SO2 and Sulphur Trioxide SO3
Selection of Stainless Steel for Handling Phosphoric Acid H3PO4
Selection of Stainless Steel for Handling Hydrofluoric Acid HF
Selection of Stainless Steel for Handling Citric Acid C3H4OH (COOH)3
Selection of Stainless Steel for Handling Ammonia NH3
Selection of Stainless Steel for Handling Chlorine Cl2 and Chlorine Dioxide ClO2
Selection of Stainless Steels For Handling Hydrochloric Acid HCl
Selection of Stainless Steel for Handling Sulphuric Acid H2SO4
Selection Stainless Steel for Handling Sodium Hydroxide NaOH
Selection of stainless steels for handling acetic acid (CH3COOH)
Selection of stainless steels for handling sodium hypochlorite (NaOCl)
Selection of stainless steels for handling nitric acid (HNO3)
NACE MR 0175/ISO 15156 for Corrosion Resistant Alloys for Sulphide Service
Selection of stainless steels in water supply and waste water treatment
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