Choosing Alloys for Chemical Processing

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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## 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.