Short answer: Pitting attacks exposed stainless steel at isolated points; crevice corrosion develops inside shielded gaps; and stress corrosion cracking requires a susceptible material, tensile stress and a specific environment. Grade, water chemistry, temperature, geometry, fabrication and stress must be reviewed together.
Stainless steel earns its corrosion resistance from a passive chromium-rich oxide film. That film can reform when damaged, which is why stainless steels perform so well in many environments. But the passive film is not invincible. In real equipment, failures often begin at local sites where chemistry, geometry and stress create conditions far more aggressive than the bulk process fluid suggests.
Three mechanisms deserve special attention: pitting corrosion, crevice corrosion and stress corrosion cracking. They are dangerous because they can progress with little general metal loss. A vessel or component may look largely clean while a local pit, crevice or crack advances toward leakage.
This is why corrosion-resistant alloy selection must consider the equipment detail, not only the chemical name of the process fluid. Chloride concentration, temperature, deposits, gasketed joints, stagnant zones, weld quality and residual stress can all decide whether a grade has enough margin.
Key Points
Important distinctions
- Pitting is localized passive-film breakdown on an exposed surface.
- Crevice corrosion is intensified inside shielded gaps where chemistry can concentrate and acidify.
- Stress corrosion cracking requires a susceptible material, tensile stress and a specific environment.
- General corrosion rate alone can underestimate the failure risk of stainless equipment.
What is the difference between pitting and crevice corrosion?
The main difference is location. Pitting starts at isolated points on an exposed surface after local breakdown of the passive film. Crevice corrosion starts inside a shielded gap—such as beneath a gasket, washer, deposit, lap joint or incomplete weld—where restricted oxygen and mass transfer allow chloride concentration and acidification. Both are forms of localized corrosion, but crevice control must also address the geometry that creates the shielded zone.
For alloy comparison, see 304 stainless steel, 316L stainless steel, 2205 duplex stainless steel and 2507 super duplex stainless steel. PREN can help rank potential pitting resistance, but it is not a service-life guarantee and cannot replace review of weld condition, surface finish, geometry and actual process chemistry.
Pitting: small initiation sites, large consequences
Pitting begins when the passive film breaks down at a local weak point. Chlorides are a common driver because they destabilize the passive film and support local acidification inside the pit. Once a pit becomes active, its internal chemistry can become more aggressive than the outside environment, allowing the pit to propagate even when the surrounding surface remains passive.
Molybdenum-bearing grades such as 316L resist pitting better than 304 in many chloride environments, and duplex or super duplex grades can offer a higher margin. But alloy content is only part of the story. Surface roughness, heat tint, embedded iron, weld scale and deposits can all create initiation sites. A poorly cleaned high-alloy component may perform worse than expected.
Crevice corrosion: geometry creates its own chemistry
Crevice corrosion is often more severe than open-surface pitting because the gap restricts oxygen and mass transfer. Under a gasket, lap joint, washer, deposit or tight fixture, the local solution can become depleted in oxygen, enriched in chlorides and lower in pH. The material outside the crevice may still look healthy while the shielded area corrodes aggressively.
This mechanism explains why design details matter. If the service environment contains chlorides, avoid unnecessary crevices, improve drainage, use welds rather than overlapping joints where appropriate, and specify cleaning procedures that prevent deposits. Alloy upgrades help, but they do not remove the need for good geometry.
Failure mechanism comparison
| Mechanism | Typical trigger | Design response |
|---|---|---|
| Pitting | Chloride, heat tint, surface contamination, stagnant droplets | Select higher pitting resistance, improve surface finish and passivation. |
| Crevice corrosion | Gaskets, deposits, lap joints, threaded zones | Reduce crevices, improve drainage, choose more resistant alloy where geometry cannot change. |
| Stress corrosion cracking | Tensile stress plus chloride and temperature | Control residual stress, temperature and alloy family; consider duplex or super duplex stainless steel when needed. |
The same component can experience more than one mechanism. Field failure analysis should not assume a single cause too early.
Stress corrosion cracking: why a strong-looking part can fail suddenly
Stress corrosion cracking is especially serious because it combines mechanical stress and environment. Tensile stress may come from service load, forming, welding residual stress, cold work or assembly fit-up. In chloride-containing environments, austenitic stainless steels can become susceptible as temperature and stress increase.
The crack path may be narrow and difficult to detect until leakage or fracture occurs. Reducing risk can involve stress relief where appropriate, improved welding practice, avoiding cold-worked high-stress regions, changing geometry, lowering temperature or selecting an alloy family with better resistance. In many cases the answer is not simply "more chromium"; it is a more complete control of material, stress and environment.
Why can stainless steel show weaknesses in a new chiller room?
A new chiller room does not automatically provide a benign corrosion environment. Possible contributors include chlorides or oxidizing treatment chemicals, stagnant commissioning water, dead legs, gaskets or threaded joints, weld heat tint, fabrication contamination, wet insulation, condensation and residual tensile stress. Review the failure location, water analysis, maximum operating and cleaning temperatures, treatment chemicals, flow history, joint geometry, weld condition, insulation and installed grade before changing materials.
What should buyers compare when selecting a stainless steel grade?
| Grade family | General selection direction | Important qualification |
|---|---|---|
| 304/304L | Common starting point for many moderate service environments | Do not select from the grade name alone when chlorides, deposits, crevices or aggressive cleaning are present |
| 316/316L | Molybdenum addition generally improves pitting resistance compared with 304/304L | It is not universally resistant to chloride pitting, crevice corrosion or SCC |
| 2205 duplex | Can provide a higher localized-corrosion and chloride-SCC resistance margin than common austenitic grades | Welding procedure, product condition, temperature, environment and applicable specification still require review |
| 2507 super duplex | Considered for more severe chloride-bearing service where additional margin is needed | Selection and fabrication require application-specific engineering review; a higher alloy grade cannot correct poor geometry or surface condition |
This table gives selection direction, not engineering approval. Laboratory rankings such as PREN, critical pitting temperature (CPT) and critical crevice temperature (CCT) compare alloys under defined test conditions; they do not reproduce every operating environment.
Checklist
Corrosion review questions
- What is the maximum operating and cleaning temperature?
- Are chlorides, acids, oxidizers or reducing species present?
- Are there gaskets, deposits, dead zones or lap joints?
- Will welding leave heat tint or require pickling/passivation?
- Is the component under sustained tensile stress?
- What is the inspection access and consequence of leakage?
- Is field cleaning likely to introduce chlorides or concentration cycles?
Frequently asked questions
What is stainless steel localized corrosion?
Localized corrosion attacks limited areas rather than thinning the whole exposed surface at a similar rate. Pitting and crevice corrosion are common localized mechanisms; stress corrosion cracking develops as cracks under the combined action of material susceptibility, tensile stress and a specific environment.
Is crevice corrosion the same as pitting corrosion?
No. Pitting forms on an exposed surface. Crevice corrosion develops in a shielded gap where restricted transport changes the local chemistry.
Can stainless steel corrode in a new chiller room?
Yes. New equipment can still contain weld heat tint, fabrication contamination, residual stress, stagnant commissioning water, wet insulation or chloride-bearing treatment chemicals. Diagnose the mechanism before changing the grade.
Does 316L prevent pitting and crevice corrosion?
No grade is universally resistant. Compared with 304, 316L generally offers improved pitting resistance in many chloride environments, but temperature, chemistry, crevice geometry, welding, finish and cleaning still affect performance.
References and Evidence Notes
1. worldstainless — Corrosion properties. Supports the passive-film explanation and localized-corrosion classifications.
2. British Stainless Steel Association — Principles and prevention of crevice corrosion. Supports the crevice chemistry, typical locations and geometry controls.
3. Nickel Institute — Piping Manual for Stainless Steel Pipes for Buildings. Supports the building-piping discussion of water quality, pitting, crevice corrosion and chloride-related SCC.