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Corrosion

Selection Stainless Steel for Handling Sodium Hydroxide NaOH






Sodium Hydroxide (Caustic Soda) is a strong base. It is used in metal degreasing and cleaning processes in a wide range of industry applications.

Stainless steel types 304 and 316 can be considered resistant below 80 degC, up to the limit of solubility.

Both 304 and 316 stainless steel types are resistant to a wide range of concentration and temperature. Below 80 degC they can be considered resistant to any concentration of sodium hydroxide, up to the limit of solubility. There can be a risk of stress corrosion cracking (SCC) attack at higher temperatures, which is common to both the 304 and 316 types.

Corrosion resistance of stainless steel

The iso-corrosion diagram 0.1mm/year lines for 304 and 316 types coincide (purple).

(The broken line represents the boiling point)

The iso-corrosion diagram 0.1mm/year lines for 304 and 316 types coincide

This should not be an issue if service temperatures are limited to a 95 degC maximum.



Risk of stress corrosion cracking attack

'Caustic stress corrosion cracking' occurs at higher temperatures than chloride stress corrosion cracking (which can occur at temperatures as low as 60 degC).
The area of risk in sodium hydroxide is shown on the iso-corrosion diagram by the area bounded by a green line.

Risk of pitting attack by chlorides

Chlorides should not pose as great a pitting and crevice corrosion attack threat in sodium hydroxide as they do in acid solutions.
The high pH values of the 'basic' sodium hydroxide helps arrest the normal mechanisms of attack.

Care may be necessary when selecting 304 types for sodium hydroxide cleaning systems or tanks, where 'carry-over' of chlorides could occur from prior treatment stages. It may be better to consider 316 or the 316L types if this could occur. The 316L type may be a marginally better choice where the steel may have been sensitised in the heat-affected zone (HAZ) of welds and post weld softening / stress relief is not practical.

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Related References:
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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