## The Selection Process
1. Define the environment (acid type, concentration, temperature, contaminants)
2. Consult isocorrosion diagrams (0.1 or 0.5 mm/year curves)
3. Consider upset conditions (worst-case temperature, concentration spikes)
4. Evaluate economics (cheap alloy + corrosion allowance vs expensive alloy + long life)
## Alloy Selection by Acid Type
### Sulfuric Acid
| Concentration | Alloy | Notes |
|-------------|-------|-------|
| 0-5% (dilute) | 316L, Alloy 20 | Aeration increases attack |
| 5-85% | Alloy 20 (UNS N08020) | The classic sulfuric acid alloy (35Ni-20Cr-3.5Cu-2.5Mo) |
| 85-98% | Carbon steel | Passive film in concentrated H2SO4 |
### Hydrochloric Acid
The most aggressive common acid. Up to 40 degrees C: Hastelloy B-3 or C-276. Tantalum is immune at all concentrations below 150 degrees C. Non-metallic linings (PTFE, glass) are widely used.
### Nitric Acid
An oxidizing acid. 304L stainless is the standard up to 65% at boiling. Nickel alloys (Alloy 600) are NOT suitable.
## Caustic Service (NaOH, KOH)
Below 50 degrees C: carbon steel. 50-120 degrees C: stress-relieved carbon steel. Above 120 degrees C: Nickel 200 or Monel 400.
## Clad Construction
For large vessels, explosion-clad or weld-overlay construction provides carbon steel strength with CRA liner corrosion resistance at a fraction of solid CRA cost. Common combinations: carbon steel + 316L, carbon steel + Alloy 625, carbon steel + Alloy 20.
Choosing Alloys for Chemical Processing
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Chemical plants process acids, alkalis, and reactive gases at elevated temperatures. Alloy selection is driven by isocorrosion diagrams, process upset conditions, and the economics of corrosion allowance versus premium alloys.
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